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Potential hydrogen levels

The distinction between potential hydrogen levels and weld hydrogen levels was explained in Chapter 1, and this appendix provides the required details. The procedures for making such measurements are described in Appendix B. It is emphasised that both this discussion of typical hydrogen levels and also prediction procedures explained in the main text are based on ... [Pg.102]

A1 Typical potential hydrogen levels (moisture levels in coatings and fluxes). (Heights of curves indicate relative frequency of test results for each type of consumable.)... [Pg.103]

Char formation and reduced monomer production are observed for all of these additives upon reaction with PMMA. Char formation increases as a function of temperature, for the hydrido cobalt compound, there is 5% char at 262°, 8.5% at 322°, 15% at 338°, and 19% at 375°C the cobalt(lll) cyanide produces 3% char at 338° and 11% at 375°C the cobalt(ll) cyanide yields 11% char at 375°C. At the highest temperature, 375°C, the amount of monomer formation is 22% for K3Co(CN)5, 11% for K3Co(CN)6, and 10% for HCo[P(OPh)3]4. Ideally one would hope to observe no monomer formation and complete char production. Such is not the case here, these materials probably have no utility as flame retardant additives for PMMA since monomer formation, even at a reduced level, will still permit a propagation of the burning process. While somewhat positive results for these three additives do not prove the validity of the hypothesis, we take this to be a starting point in our search for suitable additives, further work is underway to refine the hypothesis and to identify other potential hydrogenation catalysts and other additives that may prove useful as flame retardants for PMMA... [Pg.186]

The SSCHISM infrastructure model calculates the cost of the potential hydrogen pathway-supply options shown in Table 15.3 for 73 of the largest US urbanised areas and selects the cheapest supply pathway in each city at a specified market penetration. The cheapest pathway choice for any given city depends on the size of the city, level of demand, demand density, and local energy and feedstock prices. [Pg.468]

The spectroscopic dissociation energy D is the dissociation energy of an ideal gas molecule at absolute zero, where all the gas molecules are in the zero potential energy level, h is Planck s constant (6.62 x lO Vrg second), and iv, is the frequency of vibration of the nuclei at the lowest vibrational level, which is above the point of zero potential energy at the equilibrium intemuclear separation. Thus, for the hydrogen molecule. D — 4.476 electron volts, l o = 1.3185 x IO 1 sec1, and since I electron volt = 23.06 kilocalories per mole wc calculate I) using Hq.(21) as... [Pg.500]

The reduction potentials for various alkyl halides range from +0.5 to +1.5 V therefore, when Fe° serves as an electron donor, the reaction is thermodynamically favorable. Because three reductants are present in the treatment system (Fe°, H2, and Fe2+), three possible pathways exist. Equation (13.9) represents the oxidation of Fe° by reduction of a halogenated compound. In the second pathway, the ferrous iron behaves as a reductant, as represented in Equation (13.10). This reaction is relatively slow because the ability to reduce a pollutant by ferrous iron is dependent on the speciation ferrous ions, which is determined by the ligands present in the system. The third possible pathway, Equation (13.11), is dehalogenation by hydrogen. This reaction does not occur easily without a catalyst. In addition, if hydrogen levels become too high, corrosion is inhibited (Matheson and Tratnyek, 1994) ... [Pg.513]

Many of the applications in which CEs are involved require clarity or uniform properties on a microscopic structural level, so miscibility or molecular-scale mixing is important when CE-based blends are formed. There are some examples of miscible or homogeneous CE blends with vinyl polymers. One interesting class of these is a mixture of CE and poly(vinyl phenol) (PVPh) [101,102], This phenolic polymer is known to form a miscible blend with a wide variety of polymers with potential hydrogen-bond-accepting groups [101], the latter set including commercially available CEs, i.e., cel-... [Pg.119]

Assuming the feedstock is methane, which is the major component of natural gas, the theoretical feed requirement would be equivalent to one-fourth of the potential hydrogen production or 16,713 SCF CH /ST NH3(15.2 MM BTU/ST). However, the actual process consumes on the order of 22,420 SCF CHi+/ST NH3 or about 20.4 MM BTU/ST NH3 (LHV). The required quantity of feed depends on the process design criteria chosen for the methane conversion in the reforming section, the efficiency of CO conversion, degree of CO2 removal and the inerts (CHi+ + Ar) level maintained in the ammonia synthesis loop. Thus, the potential hydrogen conversion efficiency of the feedstock in the steam reforming process is about 75%. Table 3 shows where the balance of the feed is consumed or lost from the process. [Pg.67]

With mild steel and C-Mn steels the hydrogen potential of the welding process must be known so that the welding diagram can be entered via the correct CE axis. Detailed information on typical hydrogen levels for different processes is given in Appendix A. [Pg.38]

Other testing procedures are used to produce information on potential and weld hydrogen levels because of the demand for simpler methods for production control purposes. Such methods may not necessarily afford adequate precision, and it is recommended that any decisions regarding welding procedure or comparison of consumables should be based on information provided by the standard tests, or methods calibrated to them. [Pg.102]

Figure Al compares moistures levels of electrode coatings and submerged-arc fluxes. (The histograms show the relative frequency of measurements over the total range.) Typical levels of moisture in both agglomerated and fused submerged-arc fluxes are shown, hut it is emphasised that in this process the filler wire is an additional source of potential hydrogen. Figure Al compares moistures levels of electrode coatings and submerged-arc fluxes. (The histograms show the relative frequency of measurements over the total range.) Typical levels of moisture in both agglomerated and fused submerged-arc fluxes are shown, hut it is emphasised that in this process the filler wire is an additional source of potential hydrogen.
A3 General relationships between potential hydrogen and weld metal hydrogen levels. [Pg.105]


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