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Bases ammonia

Conclusions - Dissolved Oxygen. Continued attainment of DO standards in the Willamette Basin in the face of a current regional growth rate of 1% yr will require continued augmentation of flow as well as pollution control, particularly with respect to ammonia. Based on model results discussed, there appears to be little justification for the installation of advanced wastewater treatment systems in the basin for the purpose of maintaining acceptable DO levels. [Pg.265]

Reducing smelting furnaces that produce a high-sulfidity, kraft-like green liquor are now employed at sodium-based sulfite mills. U.S. EPA anticipates that it would be necessary to replace the existing recovery boilers at ammonia-based mills if chemical substitution to a sodium base were employed. Additionally, it is likely that, because the heat value of sodium spent liquor is lower than ammonia spent liquor, evaporator modification may he required if excess capacity does not already exist. [Pg.892]

A review of processes for leaching of base metals from their ores has appeared recently.2 Recent developments involving the generation and composition of sulfate-, chloride-, or ammonia-based streams which are used to feed solvent extraction processes are considered briefly below. [Pg.766]

Table 18. Sensor layer for ammonia based on a lipophilic pH indicator dye in silicone. Table 18. Sensor layer for ammonia based on a lipophilic pH indicator dye in silicone.
The members of Wolfbeis team constructed an optical sensor for ammonia-based on ion pairing76. They immobilized pH-sensitive dye (bromophenol blue) as an ion pair with cetyltrimethylammonium bromide (CTABr) in a silicone polymer matrix. Bromophenol blue, while contact the ammonia (both in water as well as in gaseous form) changes its color reversibly from yellow to blue. The immobilized dye shows long wave absorption with a good photostability. [Pg.370]

Alstom, Press Releases, Alstom and Statoil to jointly develop project for chilled ammonia-based C02 capture for natural gas in Norway, http //www.alstom.com/pr corp/2007/corp/43066.EN. php languageId=EN dir=/pr corp/2007/corp/ idRubriqueCourante=15445, June 21, 2007. [Pg.597]

In an ammonia-based solution, the solution pH can vary between 7 (for an extremely diluted NH3 solution) and 11.5 (for an NH3 concentration of 1.2M).36 The equilibrium reactions suggest that, in an ammonia solution, a Zn2+ ion in the solution will stay in the form of Zn(OH)2 along with Zn (NH3)2, whereas a Cd2+ ion in an ammonia solution is predominantly Cd(NH3)4+. [Pg.204]

At the beginning of this decade, Zewail and coworkers reported a fundamental work of solvation effect on a proton transfer reaction [195]. a-naphthol and n-ammonia molecules were studied in real-time for the reaction dynamics on the number of solvent molecules involved in the proton transfer reaction from alcohol towards the ammonia base. Nanosecond dynamics was observed for n=l and 2, while no evidence for proton transfer was found. For n=3 and 4, proton transfer reaction was measured at pisosecond time scale. The nanosecond dynamics appears to be related to the global cluster behavior. The idea of a critical solvation number required to onset proton transfer... [Pg.329]

The reaction of borontrifluoride (acid) with ammonia (base) results into a stable octet configuration between mutual sharing of a pair of electrons of latter (donor) and former (acceptor). [Pg.97]

Thus the last column in Tables 1 and 2 corresponds to the volatility ratio of ammonia based on free ammonia and extrapolated to zero concentration of free ammonia. This number should be independent of the concentrations studied at a given temperature, and... [Pg.197]

Ou et al. [74] reported the enhancement of the degradation of methyl bromide in soil pretreated with an ammonia-based nitrogen fertilizer (i. e., (NH4)2S04) and stimulation of methyl bromide degradation in soil inoculated with a nitrifier, Nitrosomonas europaea. [Pg.390]

Multiple publications (Pankow et al. 1997 Ingebrethsen et al. 2001 Pankow et al. 2003 Watson et al. 2004) have discussed measuring free-base nicotine directly, addressed the importance of free-base nicotine delivery, and examined the chemical properties of nicotine in cigarette smoke as an important determinant of the effective delivery and bioavailability of nicotine from cigarettes. Pankow et al. (1997) examined how ammonia influences nicotine delivery in tobacco smoke and concluded that conversion of nicotine to the free-base form could be facilitated by ammonia. Based on a theoretical treatment, Pankow et al. (1997) concluded that, under certain circumstances, up to 40% of the nicotine could be available as the volatile free-base form. These authors also concluded that the rate of volatilization was more rapid than that previously measured by Lewis et al. (1995) using denuder technology to examine the properties of mainstream cigarette smoke. [Pg.449]

Katada, N., Igi, H., Kim, J.H., and Niwa, M. (1997) Determination of the acidic properties of zeolite by theorecti-cal analysis of temperature programmed desorption of ammonia based on adsorption equilibrium. J. Phys. Chem. B, 101, 5969-5977. [Pg.171]

Parameter Ammonia base mill Sodium base mill Magnesium base mill Calcium base mill ... [Pg.461]

When large amounts of copper deposits in boiler mbes cannot be removed with hydrochloric acid due to the relative insolubility of copper, ammonia-based oxidizing compounds have been effective. Used in a single separate stage, the ammonia sodium bromate step includes the introduction into the boiler system of solutions containing ammonium bromate to rapidly oxidize and dissolve the copper. [Pg.585]

Extrapolation to HF- or Ammonia-based ehemistries is not directly possible. In each of these cases, the equilibria must be recomputed taking... [Pg.187]

Fig. 18. PECVD TEOS oxide slurry removal efficiency in ammonia-based chemistries (0.25, 6) performed at 55°C during 10 min. Diluted ammonia with megasonics gives results as good as the scrubber. Fig. 18. PECVD TEOS oxide slurry removal efficiency in ammonia-based chemistries (0.25, 6) performed at 55°C during 10 min. Diluted ammonia with megasonics gives results as good as the scrubber.
The single largest use of ammonia is its direct apphcation as fertdizer, and in the manufacture of ammonium fertilizers that have increased world food production dramatically. Such ammonia-based fertilizers are now the primary source of nitrogen in farm soils. Ammonia also is used in the manufacture of nitric acid, synthetic fibers, plastics, explosives and miscellaneous ammonium salts. Liquid ammonia is used as a solvent for many inorganic reactions in non-aqueous phase. Other apphcations include synthesis of amines and imines as a fluid for supercritical fluid extraction and chromatography and as a reference standard in i N-NMR. [Pg.19]

Ammonia-based chemicals appear to have some advantages over sodium systems. They are less costly, and regeneration by conventional means is possible, with the byproduct, ammonium sulfate, a marketable commodity for fertilizer. [Pg.1330]

Fig. 9.25 Hollow waveguide for ammonia, based on capillary coated with oxazine perchlorate (adapted from Giuliani et al., 1983)... Fig. 9.25 Hollow waveguide for ammonia, based on capillary coated with oxazine perchlorate (adapted from Giuliani et al., 1983)...
Evidence of this behavior was reported by Webb, Singer and Nazaroff (2002). They opened a bottle of an ammonia-based cleaning solution in a room that had been preconditioned with 3200 mg of nicotine. They observed an immediate increase in the gas-phase nicotine concentration that they ascribed to conversion of nonvolatile nicotine salts to semi-volatile free-base nicotine. [Pg.318]

Today s coke plant gas purification processes are mostly carried out under atmospheric pressure, employing a circulated ammonia-based absorbent. The consumption of the external solvent is reduced via the use of ammonia available in the coke gas (138). An example of innovative purification processes is the ammonia hydrogen sulfide circulation scrubbing (ASCS) (Figure 17), in which the ammonia contained in the raw gas dissolves in the NH3 absorber and then the absorbent saturated with the ammonia passes through the H2S absorber to selectively absorb the H2S and HCN components from the coke gas. The next step is the thermal regeneration of the absorbent with the steam in a two-step desorption plant, whereas a part of the deaciditied water is fed back into the H2S absorber (25). [Pg.344]

Alstom Environment Control Systems Alstom and Statoil to jointly develop project for chilled ammonia-based C02 capture for natural gas in Norway. [Pg.217]

Since the purpose of this report is primarily to interpret the behavior of the wood-ammonia system and to relate it to practical application, we will first briefly review current methods of forming wood. We will discuss in some detail methods of softening wood with water and heat and the molecular changes underlying them and then extend these concepts to explain the more complicated but similar ammonia-based systems, and their possible practical implications. [Pg.335]

While the development of flue gas clean-up processes has been progressing for many years, a satisfactory process is not yet available. Lime/limestone wet flue gas desulfurization (FGD) scrubber is the most widely used process in the utility industry at present, owing to the fact that it is the most technically developed and generally the most economically attractive. In spite of this, it is expensive and accounts for about 25-35% of the capital and operating costs of a power plant. Techniques for the post combustion control of nitrogen oxides emissions have not been developed as extensively as those for control of sulfur dioxide emissions. Several approaches have been proposed. Among these, ammonia-based selective catalytic reduction (SCR) has received the most attention. But, SCR may not be suitable for U.S. coal-fired power plants because of reliability concerns and other unresolved technical issues (1). These include uncertain catalyst life, water disposal requirements, and the effects of ammonia by-products on plant components downstream from the reactor. The sensitivity of SCR processes to the cost of NH3 is also the subject of some concern. [Pg.164]

A preliminary-level economic evaluation (13) performed by EPRI (Electric Power Research Institute) and TVA (Tennessee Valley Authority) indicates that a combination of electrostatic precipitators (or bag house), ammonia-based SCR system, and wet lime/limestone FGD scrubber range between 20% to 185% cheaper than wet process for complete control of particulates, N0X and S02 The lower percentage is for the second type and higher percentage for the first type of process. Therefore, the second type of process appears to be more promising and will be the subject of further discussion in this paper. [Pg.166]

Ammonia-based liquors, when incinerated, result in a loss of nitrogen as N2 in the flue gas. This difficulty is highly responsible for the domination of Kraft pulping. Magnesium-based liquor incineration is most easily accomplished, and can be achieved either in a Tomlinson furnace or a Copeland fluidized bed system. [Pg.450]


See other pages where Bases ammonia is mentioned: [Pg.149]    [Pg.273]    [Pg.530]    [Pg.7]    [Pg.59]    [Pg.32]    [Pg.395]    [Pg.117]    [Pg.271]    [Pg.13]    [Pg.53]    [Pg.60]    [Pg.461]    [Pg.211]    [Pg.220]    [Pg.113]    [Pg.502]    [Pg.174]    [Pg.185]    [Pg.233]    [Pg.3]    [Pg.288]    [Pg.159]   
See also in sourсe #XX -- [ Pg.30 , Pg.31 ]




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