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Pretreatment for

An alternative pretreatment for seawater is acidification of the bicarbonate followed by degasification to remove the carbon dioxide generated. The precipitation step for the seawater process is given by (76) ... [Pg.348]

The success of a reverse osmosis process hinges direcdy on the pretreatment of the feed stream. If typical process streams, without pretreatment to remove partially some of the constituents Hsted, were contacted with membranes, membrane life and performance would be unacceptable. There is no single pretreatment for all types of foulants. Pretreatment methods range from pH control, adsorption (qv), to filtration (qv), depending on the chemistry of the particular foulant. Some of the pretreatment methods for each type of foulant are as foUow (43—45) ... [Pg.150]

Aerobic treatment is generally appHed to lower strength wastewaters, whereas anaerobic treatment is employed as a pretreatment for high strength wastewaters. The choice of process depends both on the concentration of organics and the volume of wastewater to be treated. [Pg.185]

Chemical Oxidation. Chemical oxidation can be appHed ia iadustrial wastewater pretreatment for reduction of toxicity, to oxidize metal complexes to enhance heavy metals removal from wastewaters, or as a posttreatment for toxicity reduction or priority pollutant removal. [Pg.192]

Cupric ion concentration is kept at an acceptable but low level by direct air oxidation of the solution. SoHds formation from sulfides in the feed gas is also possible therefore, pretreatment for sulfur removal is required. [Pg.55]

Eor the cover-coat direct-on process, a ferric sulfate [10028-22-5] Ee2(S0 2> etch is included in the metal pretreatment for rapid metal removal. It is designed to remove ca 20 g/m (2 g/ft ) of iron from the sheet metal surface. Hydrogen peroxide [7722-84-1/, H2O2, is added intermittently to a 1% ferric sulfate solution to reoxidize ferrous sulfate [7720-78-7] EeSO, to ferric sulfate. [Pg.212]

Toxicity. Low toxicity from solvent-vapor inhalation or skin contac t is preferred because of potential exposure during repair of equipment or while connections are being broken after a solvent transfer. Also, low toxicity to fish and bioorganisms is preferred when extraction is used as a pretreatment for wastewater before it enters a biotreatment plant and with final effluent discharge to a stream or lake. Often solvent toxicity is low if water solubility is high. [Pg.1460]

Pretreatment For most membrane applications, particularly for RO and NF, pretreatment of the feed is essential. If pretreatment is inadequate, success will be transient. For most applications, pretreatment is location specific. Well water is easier to treat than surface water and that is particularly true for sea wells. A reducing (anaerobic) environment is preferred. If heavy metals are present in the feed even in small amounts, they may catalyze membrane degradation. If surface sources are treated, chlorination followed by thorough dechlorination is required for high-performance membranes [Riley in Baker et al., op. cit., p. 5-29]. It is normal to adjust pH and add antisealants to prevent deposition of carbonates and siillates on the membrane. Iron can be a major problem, and equipment selection to avoid iron contamination is required. Freshly precipitated iron oxide fouls membranes and reqiiires an expensive cleaning procedure to remove. Humic acid is another foulant, and if it is present, conventional flocculation and filtration are normally used to remove it. The same treatment is appropriate for other colloidal materials. Ultrafiltration or microfiltration are excellent pretreatments, but in general they are... [Pg.2037]

The liquid was applied and dried on cellulose filter (diameter 25 mm). In the present work as an analytical signal we took the relative intensity of analytical lines. This approach reduces non-homogeneity and inequality of a probe. Influence of filter type and sample mass on features of the procedure was studied. The dependence of analytical lines intensity from probe mass was linear for most of above listed elements except Ca presented in most types of filter paper. The relative intensities (reduced to one of the analysis element) was constant or dependent from mass was weak in determined limits. This fact allows to exclude mass control in sample pretreatment. For Ca this dependence was non-linear, therefore, it is necessary to correct analytical signal. Analysis of thin layer is characterized by minimal influence of elements hence, the relative intensity explicitly determines the relative concentration. As reference sample we used solid synthetic samples with unlimited lifetime. [Pg.370]

In a typical process for manufacture on a commercial scale bleached wood pulp or cotton linters are pretreated for 12 hours with 40-50% sulphuric acid and then, after drying, with acetic acid. Esterification of the treated cellulose is then carried out using a mixture of butyric acid and acetic anhydride, with a trace of sulphuric acid as catalyst. Commercial products vary extensively in the acetate/ butyrate ratios employed. [Pg.628]

Fig. 4. Example.s of rough surfaces pretreated for adhesive bonding (a) microtibrous oxide on copper (cf. 29J) (b) a dendritic zinc surface (cf. [30J). Fig. 4. Example.s of rough surfaces pretreated for adhesive bonding (a) microtibrous oxide on copper (cf. 29J) (b) a dendritic zinc surface (cf. [30J).
Aluminium coatings also provide a suitable key or pretreatment for subsequent coatings, e.g. aluminised steel provides a good base for vitreous enamel. [Pg.476]

New pretreatments for aluminium to enable it to be nickel plated more easily have led to novel decorative applications including large mirrors. Wyszynski has described a proprietary process applicable to a wide range of aluminium alloys. [Pg.540]

Pretreatment for FT boilers designed for industrial duty becomes slightly more exacting because these typically operate at about 85 to 100 psig/114.7 psia (338 °F/169.9 °C) perhaps up to, say, 250 to 300 psig (264.7-314.7 psia). [Pg.192]

Fe electrodes with electrochemically polished (cathodically pretreated for 1 hr) and renewed surfaces have been investigated in H20 + KF and H20 + Na2S04 by Rybalka et al.721,m by impedance. A diffuse-layer minimum was observed at E = -0.94 V (SCE) in a dilute solution of Na2S04 (Table 19). In dilute KC1 solutions E,njn was shifted 40 to 60 mV toward more negative potentials. The adsorbability of organic compounds (1-pentanol, 1-hexanol, cyclohexanol, diphenylamine) at the Fe electrode was very small, which has been explained in terms of the higher hydro-philicity of Fe compared with Hg and Hg-like metals. [Pg.123]

The examples that are treated below are those sequences where all steps - except the last — are preparations for a color or fluorescence derivatization reaction which is carried out in the last step, i. e. they can be regarded as a sort of selective in situ pretreatment for a final detection reaction. Such reaction sequences are frequently necessary because all the reagents cannot be mixed together in a single solvent, or because it is necessary to dry, heat or irradiate with UV light between the individual reaction steps. The detection of aromatics by the reaction sequence nitration — reduction — diazotization - couple to form an azo dye is an example of this type (Fig 21). [Pg.37]

Concern has been expressed about the possible formation of dioxins and furans. However, measurements during experiments indicated that the emissions of dioxins and furans were not significantly elevated. Dioxin emissions with or without plastic input appeared to be about a factor of 100 below the standard of 0.1 ng/Nm TEQ TCCD (toxicity equivalent in relation to the toxic dioxin TCCD) (a.7). This might be due to the benefit of the strongly reducing atmosphere and the high temperature of 2100 °C. In total, until now the conclusion has been that at current PVC levels in MSW, pretreatment for chlorine removal is unnecessary. [Pg.9]

To use the DFT properly for evaluating normal surface deformation, the linear convolution appearing in Eq (27) has to be transformed to the circular convolution. This requires a pretreatment for the influence coefficient Kj and pressure pj so that the convolution theorem for circle convolution can be applied. The pretreatment can be performed in two steps ... [Pg.123]

Brewis D.M. and Dahm R.H., 2003, Mechanistic studies of pretreatments for elastomers, in Proceedings of Swiss Bonding 2003, Zurich, 69-75. [Pg.772]

Superficial salicylic acids have been shown to be safe and efficacious for treatment of PIH. In a study of five patients with Fitzpatrick s Skin Types V and VI with PIH, pretreatment for 2 weeks with hydroquinone 4% cream followed by a series of five 20-30% salicylic acid chemi-... [Pg.181]

Some part of the cellulose fraction is redirected to make cellulose derivatives, such as cellulose acetate, methyl and ethyl cellulose, carboxymethyl cellulose, hydroxyethyl cellulose, and hydroxypropyl cellulose. These derivatives find multiple applications, for instance, as additives in current products (e.g., paints, lacquers) of chemical industry. Typically, the preparation of cellulose derivatives takes place as a two-phase reaction cellulose is pretreated, for example, with alkali, and a reagent is added to get the substitution. Usually no catalyst is needed [5]. [Pg.165]

Figure 3. Relationship between levels of protein kinase C and inhibition of EGF binding to Swiss 3T3 cells by PDBu and palytoxin. Confluent quiescent Swiss 3T3 cells were pretreated for 72 hr with 0.1% FCS plus solvent ( ), 20 nM PDBu (o), 200 nM PDBu (A), or 2000 nM ( ). Cells were then washed and treated with either 200 nM PDBu (A) or 11 pM palytoxin (B) for the times shown and assayed as in Figure 1. Other conditions were as described in the legend to Figure 2. The data for 200 nM PDBu are composites of two independent experiments. (Reproduced with permission from Ref. 33. Copyright 1987 Cancer Research, Inc.)... Figure 3. Relationship between levels of protein kinase C and inhibition of EGF binding to Swiss 3T3 cells by PDBu and palytoxin. Confluent quiescent Swiss 3T3 cells were pretreated for 72 hr with 0.1% FCS plus solvent ( ), 20 nM PDBu (o), 200 nM PDBu (A), or 2000 nM ( ). Cells were then washed and treated with either 200 nM PDBu (A) or 11 pM palytoxin (B) for the times shown and assayed as in Figure 1. Other conditions were as described in the legend to Figure 2. The data for 200 nM PDBu are composites of two independent experiments. (Reproduced with permission from Ref. 33. Copyright 1987 Cancer Research, Inc.)...

See other pages where Pretreatment for is mentioned: [Pg.1103]    [Pg.633]    [Pg.1036]    [Pg.251]    [Pg.277]    [Pg.212]    [Pg.409]    [Pg.2227]    [Pg.218]    [Pg.335]    [Pg.438]    [Pg.963]    [Pg.964]    [Pg.84]    [Pg.85]    [Pg.1236]    [Pg.301]    [Pg.397]    [Pg.535]    [Pg.623]    [Pg.273]    [Pg.113]    [Pg.143]    [Pg.144]    [Pg.133]    [Pg.458]   


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Aeration Towers for Makeup Water Pretreatment

Pretreatment Standards for Existing Sources

Pretreatment Standards for Existing Sources PSES)

Pretreatment Standards for New Sources

Pretreatment for Nerve Agent Exposure

Pretreatment for Rejection Increase and Fouling Prevention

Pretreatment for Steel

Pretreatment for adhesion

Pretreatment for metals

Pretreatment for nerve-agent poisoning

Pretreatment for painting (

Pretreatments for concrete

Pretreatments for polymer composites

Pyrolysis yields for pretreatments

Research for pretreatment

Sample pretreatment for voltammetric analysis

Surface Pretreatment for Structural Bonding

Textile Chemicals for Pretreatment, Dyeing and Finishing

The need for sample pretreatment

Yields for pretreatments

Yields of organic compounds pyrolysis syrups for pretreatments

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