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Feed mole ratio

A step-limited Newton-Raphson iteration, applied to the Rachford-Rice objective function, is used to solve for A, the vapor to feed mole ratio, for an isothermal flash. For an adiabatic flash, an enthalpy balance is included in a two-dimensional Newton-Raphson iteration to yield both A and T. Details are given in Chapter 7. [Pg.319]

A estimate of vapor to feed mole ratio, if known ... [Pg.320]

Single reactions. For single reactions, a good initial setting is 95 percent conversion for irreversible reactions and 95 percent of the equilibrium conversion for reversible reactions. Figure 2.9 summarizes the influence of feed mole ratio, inert concentration, temperature, and pressure on equilibrium conversion. ... [Pg.63]

UOP Inc. is the key source of technology in this area, having numerous patents and over 70 units operating worldwide (12). The dehydrogenation catalyst is usually a noble metal such as platinum. Eor a typical conversion, the operating temperature is 300—500°C at 100 kPa (1 atm) (13) hydrogen-to-paraffin feed mole ratio is 5 1. [Pg.441]

All lene Oxides and Aziridines. Alkyleneamines react readily with epoxides, such as ethylene oxide [75-21-8] (EO) or propylene oxide [75-56-9] (PO), to form mixtures of hydroxyalkyl derivatives. Product distribution is controlled by the amine to epoxide mole ratio. If EDA, which has four reactive amine hydrogens, reacts at an EDA to EO mole ratio which is greater than 1 4, a mixture of mono-, di-, tri,-, and tetrahydroxyethyl derivatives of EDA are formed. A 10 1 EDA EO feed mole ratio gives predominandy 2-hydroxyethylethylenediamine [111-41-1], the remainder is a mixture of bis-(2-hydroxyethyl)ethylenediamines (7). If the reactive NH to epoxide feed mole ratio is less than one and, additionally, a strong basic catalyst is used, then oxyalkyl derivatives, like those shown for EDA and excess PO result (8,9). [Pg.41]

Feed Mole ratio SO2/O2 Composition (mole frac.)... [Pg.212]

Table IV. Effect of Feed Mole Ratio of Propane to Oxygen0... Table IV. Effect of Feed Mole Ratio of Propane to Oxygen0...
Paushkin and Topchiev also used H3P()4-BF3 at room temperature to alkylate benzene with olefins (287,402). For alkylation of benzene with alcohols, temperatures of 90-97° and a feed mole ratio of 0.5 alcohol 1.0 benzene 0.5 catalyst were recommended (394). In a recent study (400a) these authors supplemented their previously published views (396) concerning the properties of boron fluoride complexes with phosphoric acid, alcohols, and sulfuric acid as catalysts. Data on the electroconductivity of these catalysts was correlated with their activity in alkylation of isobutane and it was concluded (400a) that the acid ion concentration did not affect the alkylation or polymerization reactions over these catalysts, and therefore the carbonium ion mechanism was not applicable. [Pg.287]

Feed mole ratio of MAA/styrene (x 102) Mole ratio of MAA/styrene in the copolymer latexb (x 02) MAA incorporated into copolymer (%) Average diameter of copolymer latexes4 (pm)... [Pg.29]

Since the Arimoto/Haven report of vinylferrocene polymerization was not detailed, this monomer was made and both its homopolymerization and its copolymerization were studied with a variety of organic comonomers such as styrene, methylacrylate, maleic anhydride, acrylonitrile, methyl methacrylate, N-vinylpyrolidone, vinyl acetate, and so on.31-38 The polymers were as well characterized as possible, and copolymer compositions were obtained versus feed mole ratios. [Pg.3]

Coil outlet pressure, psig Steam-to-feed mole ratio 10.0 —> 10.5... [Pg.165]

If the feed mole ratio of water to methane is X, and if equilibrium is achieved at reactor effluent conditions of 1073 K and 200 psia, determine the composition of the effluent gas for values of X from 1 to 10. Prepare plots of the extents of reactions (I) and (II), as well as plots of the fractions of the original CH4 that are converted to CO and CO2 versus X. [Pg.18]

Figure 4. Polymerization of epoxyethane (11, R = H) initiated with chloroaluminum tetraphenylporphyrin (1c) in CH2CI2 at room temperature. Relationship between molecular weight (Mn O), molecular-weight distribution (Mw/Mn ), and feed mole ratio of monomer to initiator ([11]o/[1c]o) at 100% monomer conversion. Figure 4. Polymerization of epoxyethane (11, R = H) initiated with chloroaluminum tetraphenylporphyrin (1c) in CH2CI2 at room temperature. Relationship between molecular weight (Mn O), molecular-weight distribution (Mw/Mn ), and feed mole ratio of monomer to initiator ([11]o/[1c]o) at 100% monomer conversion.
R= Me) initiated with manganese porphyrin (6, X = OAc) at a feed mole ratio [11]o/[6]o of 400 in the presence of MeOH at 30 C without solvent. Effects of [MeOHV[6]o on molecular weight (Mn) and molecular weight distribution (Mw/Mn). [Pg.153]

The active species of the polymerization has been considered to be a manganese alcoholate, that is formed by the insertion of the epoxide into the Mn-OAc bond of the initiator. In the presence of methanol or acetic acid, the polymerization of 11 (R = Me) has been found to proceed with immortal character, to give a narrow MWD polyether with the number of the molecule exceeding that of the initiator molecule 6 (X = OAc). An example is shown by the polymerization at a feed mole ratio of 11 (R = Me) to 6 (X = OAc) of 400 at 30 C (Figure 9), where the molecular weight of the polymer produced at 100% monomer conversion can be controlled by the mole ratio of methanol to 6 (X = OAc), while the MWD is almost constant and close to unity. Therefore, the manganese complex 6... [Pg.153]

The N alkylacrylamides were copolymerized with acrylamide via micellar copolymerization using sodium dodecylsulfate as the surfactant and potassium persulfate as the free-radical initiator. Monomer feed mole ratios were varied from 0.25 99.75 to 0.75 99.25 N-alkylacrylamide acrylamide. Following reaction, the polymers were purified by precipitation in acetone, dialysis, and lyophilization. Elemental analysis confirmed the absence of surfactant in the copolymers. [Pg.163]

In another study, lipase-catalyzed silicone polyesteramides in the bulk at 70°C under reduced pressure (10-20 mmHg) have been reported [22]. Novozym-435 was used as the enzyme under mild reaction conditions to perform the polycondensation reaction using various feed mole ratios of diethyl adipate (DBA), 1,8-octanediol (OD), and a,w-(diaminopropyl) polydimethylsiloxane (Si-NH ). The authors also synthesized poly(octamethyleneadipate), POA, and poly(a,w-(diaminopropyl) polydimethyl siloxane adipa-mide), PSiAA, using the same enzyme, and compared their properties with those of silicone polyesteramides. [Pg.21]


See other pages where Feed mole ratio is mentioned: [Pg.147]    [Pg.147]    [Pg.116]    [Pg.291]    [Pg.147]    [Pg.147]    [Pg.440]    [Pg.153]    [Pg.153]    [Pg.54]    [Pg.5784]    [Pg.7]    [Pg.54]    [Pg.169]   
See also in sourсe #XX -- [ Pg.291 ]




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