Butanol Normal

Normal butyl alcohol, propyl carbinol, n-butanol, 1-buianol, CH3CH2CH2CH2OH. B.p. 117 C. Manufactured by reduction of crotonaldehyde (2-buienal) with H2 and a metallic catalyst. Forms esters with acids and is oxidized first to butanal and then to butanoic acid. U.S. production 1978 300 000 tonnes. 

Additional evidence for carbocation intermediates in certain nucleophilic substitutions comes from observing rearrangements of the kind normally associated with such species For example hydrolysis of the secondary alkyl bromide 2 bromo 3 methylbutane yields the rearranged tertiary alcohol 2 methyl 2 butanol as the only substitution product... 

Preparation of the polymer can be carried out in glass equipment at atmospheric pressure at temperatures typically above 100°C, but the higher pressures in an autoclave result in much faster reaction rates. Each polymer molecule which used butanol as a starter contains one hydroxyl end group as it comes from the reactor diol-started polymers contain two terminal hydroxyls. Whereas a variety of reactions can be carried out at this remaining hydroxyl to form esters, ethers, or urethanes, this is normally not done and therefore lubricant fluids contain at least one terminal hydroxyl group (36). 

In petroleum and oxygenate finish removers, the major ingredient is normally acetone, methyl ethyl ketone [78-93-3], or toluene. Cosolvents include methanol, / -butanol [71-36-3], j -butyl alcohol [78-92-2], or xylene [1330-20-7]. Sodium hydroxide or amines are used to activate the remover. Paraffin wax is used as an evaporation retarder though its effectiveness is limited because it is highly soluble in the petroleum solvents. CeUulose thickeners are sometimes added to liquid formulas to assist in pulling the paraffin wax from the liquid to form a vapor barrier or to make a thick formula. Corrosion inhibitors are added to stabili2e tbe formula for packaging (qv). 

Example 2 Estimate the Critical Temperature and Critical Pressure of 2-Butanol, Which Has an Experimental Normal Boiling Point... 

Example 4 Estimate the Normal Boiling Point of 2-Butanol. 

Example 1 Estimate the critical temperature and critical pressure of 2-butanol using the Ambrose method, Eqs. (2-1) and (2-6). The experimental normal boiling point is 372.7 K. 

An example of heterogeneous-azeotrope formation is shown in Fig. 13-13 for the water-normal butanol system at 101.3 kPa. At liquid compositions between 0 and 3 mole percent butanol and between 40 and 100 mole percent butanol, the liquid phase is homogeneous. Phase sphtting into two separate liquid phases (one with 3 mole percent butanol and the other with 40 mole percent butanol) occurs for any overall hquid composition between 3 and 40 mole percent butanol. A miuimum-boihug heterogeneous azeotrope occurs at 92°C (198°F) when the vapor composition and the over l composition of the two liquid phases are 75 mole percent butanol. 

The solvent for ammonia may have an important influence. In reduction of C,o unsaturated dinitriles to primary amines over ruthenium-on-alumina, ammonia-/-butanol proved the preferred system normal alcohols gave poor rates and secondary alcohols produced N-alkylated products 18). 

Nitrobutano 1 Nitrats (Nitrobutylic Nitrate, 2-Nitro-butanol-(l)-nitrate). 02N.CH(C2H5).CH2(0N02), mw 164.12, N 17.07%, OB to C02 -68.2%, yellowish, somewhat vise liq, d 1.242g/cc at 15.5°, Prepd by Pauwels (Ref 2) by nitrating secondary nitro-normal bu-... 

Food typically is a complicated system with diverse interfaces. Stable air-water or oil-water interfaces are essential for the production of food foams and emulsions. Interface phenomena, therefore, attract great interest in the food industry. AFM provides enough resolution to visualize the interface structures, but it cannot be directly applied on air-liquid or liquid-liquid interfaces. Fortunately, the interface structure can be captured and transferred onto a freshly cleaved mica substrate using Langmuir-Blodgett techniques for AFM scan. Images are normally captured under butanol to reduce adhesion between the probe and the sample. Then, sample distortion or damage can be avoided (Morris et al, 1999). 

The initial screening of the resin catalysts was done in a batch reactor at supercritical for butene-1 conditions of temperature 155 °C, pressure of 1000 psig and at molar ratio of 1-butene water of 5.5. The reaction was stopped after predetermined period of time and the products analyzed. It was found that under the standard reaction conditions, for all of the catalysts studied, a constant concentration in the sec-butanol concentration was achieved within a 1-2 hour reaction time. Using only the linear section of the concentration-time plot, the one hour result was used to evaluate the catalyst activity, which was normalized as mmol of SBA/ per proton/ per hour (a), as mmol of product/ per gram of dry catalyst/ per hour (b) and mmol of product/ per ml of wet catalyst/ per hour (c). 

A variety of para-substituted 2-phenyl-2-butanols undergo quick and efficient reductions to the corresponding 2-phenylbutanes when they are dissolved in dichloromethane and a 2-10% excess of phenylmethylneopentylsilane and boron trifluoride is introduced at 0° (Eq. 30).126 Several reactions deserve mention. For example, when R = CF3, use of trifluoroacetic acid produces no hydrocarbon product, even after two hours of reaction time. In contrast, addition of boron trifluoride catalyst provides an 80% yield of product after only two minutes. When R = MeO, both trifluoroacetic acid and boron trifluoride produce a quantitative yield of the hydrocarbon within two minutes. However, when R = NO2, attempts to promote the reduction with either trifluoroacetic acid or even methanesulfonic acid fail even after reaction periods of up to eight hours, only recovered starting alcohol is obtained. Use of boron trifluoride provides a quantitative conversion into 2-(/ -nitrophenyl)butane after only ten minutes. It is significant that the normally easily reducible nitro group survives these conditions entirely intact.126129 Triethylsilane may be used as the silane.143... 

Cl Sulphur Black 1, which is produced from the relatively simple intermediate 2,4-dinitrophenol and aqueous sodium polysulphide. A similar product (Cl Sulphur Black 2) is obtained from a mixture of 2,4-dinitrophenol and either picric acid (6.148 X = N02) or picramic acid (6.148 X = NH2). A black dye possessing superior fastness to chlorine when on the fibre (Cl Sulphur Black 11) can be made from the naphthalene intermediate 6.149 by heating it in a solution of sodium polysulphide in butanol. An equivalent reaction using the carbazole intermediate 6.150 gives rise to the reddish blue Cl Vat Blue 43 (Hydron blue). This important compound, which also possesses superior fastness properties, is classified as a sulphurised vat dye because it is normally applied from an alkaline sodium dithionite bath. Interestingly, inclusion of copper(II) sulphate in the sulphurisation of intermediate 6.150 leads to the formation of the bluish black Cl Sulphur Black 4. 

Most of the time, enantiomers are found equally mixed together. Equally mixed enantiomers are not optically active because the rotation in one direction by one structure is canceled by the rotation in the opposite direction by the other structure. Hence, a sample of 2-butanol, for example, as normally obtained from a chemical vendor, is not optically active. An equimolar mixture of two enantiomers is called a racemic mixture and is optically inactive. Separation of a racemic mixture is not possible by conventional methods because the enantiomers are identical with respect to properties that are used to effect the separation. However, it may be possible to separate them by chemical methods, meaning that one may undergo a chemical reaction that the other does not. Some biological reactions are such reactions, and hence a single enantiomeric structure is sometimes found in nature. 

Because of their versatility and simplicity, TLC methods have been frequently applied to the separation and semi-quantitative determination of carotenoid pigments in synthetic mixtures and various biological matrices. The retention of pure carotenoid standards has been measured in different TLC systems. Separations have been carried out on silica plates using three mobile phases (1) petroleum ether-acetone, 6 4 v/v (2) petroleum ether-tert-butanol 8 2 v/v, and (3) methanol-benzene-ethyl acetate 5 75 20 v/v. Carotenoids were dissolved in benzene and applied to the plates. Developments were performed in presaturated normal chambers. The chemical structure and the Rv values of the analytes measured in the three mobile phases are listed in Table 2.1. It was concluded from the retention data that mobile phase 3 is the most suitable for the separation of this set of carotenoids [13],... 

Normal-phase TLC using a silica stationary phase was employed for the optimization of the separation of flavonoid content of Matricariae flos (Chamomilla recutita L. Rauschert). Air-dried and powdered plant material was extracted by refluxing for 10 min with methanol. The suspension was filtered, evaporated and the residue was redissolved in methanol. The mobile phases included in the experiments were 1 = ethyl acetate-methylethylketone-formic acid-water (50 30 10 10, v/v) 2 = ethyl acetate-methanol-water (75 15 10 v/v) 3 = ethyl acetate-formic acid-water (80 10 10, v/v) 4 = ethyl acetate-formic acid-water (100 20 30, v/v) 5 = ethyl acetate-formic acid-acetic acid-water (100 11 11 27, v/v) 6 = n-butanol-acetic acid-water (66 17 17, v/v) 7 = ethyl acetate-methanol-formic acid-water (75 10 5 10, v/v) 8 = ethyl acetate-acetic acid-water (80 10 10, v/v). Development was carried out in the linear ascending mode at... 

Example 2 Chromatography of nitroaniline isomers. The elution order of the nitroaniline isomers was ortho, meta, and para in normal-phase liquid chromatography using H-butanol-w-hexane mixtures as the eluent, when the stationary phase material was either silica gel, alumina, an ion-exchanger, polystyrene gel, or octadecyl-bonded silica gel. The results indicate that the separation of these compounds can be performed on a range of different types of stationary phase materials if the correct eluent is selected. The best separation will be achieved by the right combination of stationary phase material and eluent.68... 

Figure 5.2 Normal phase separation of phthalates. Column, Yanapak CN, 25 cm x 2 mm i.d. eluent, n-hexane-n-butanol (200 1) flow rate, 0.25 ml min-1 pressure, 3 MPa. Peaks 1, lauryl phthalate 2, heptyl phthalate 3, butyl phthalate 4, propyl phthalate 5, ethyl phthalate and 6, methyl phthalate.

Additional modes of HPTC include normal phase, where the stationary phase is relatively polar and the mobile phase is relatively nonpolar. Silica, diol, cyano, or amino bonded phases are typically used as the stationary phase and hexane (weak solvent) in combination with ethyl acetate, propanol, or butanol (strong solvent) as the mobile phase. The retention and separation of solutes are achieved through adsorp-tion/desorption. Normal phase systems usually show better selectivity for positional isomers and can provide orthogonal selectivity compared with classical RPLC. Hydrophilic interaction chromatography (HILIC), first reported by Alpert in 1990, is potentially another viable approach for developing separations that are orthogonal to RPLC. In the HILIC mode, an aqueous-organic mobile phase is used with a polar stationary phase to provide normal phase retention behavior. Typical stationary phases include silica, diol, or amino phases. Diluted acid or a buffer usually is needed in the mobile phase to control the pH and ensure the reproducibility of retention times. The use of HILIC is currently limited to the separation of very polar small molecules. Examples of applications... 

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