Acid-neutralization manufacturing method

Abrasive-polishing agent, use of silica gels and precipitated silicas, 625 Abrasive powder, preparation, 426, 427f Acetic acid, catalysis of silica sol-gel precursor hydrolysis, 406, 407t, 408/ Acid-neutralization manufacturing method for silica sol, procedure, 53, 54/... 

Since esterification is an equilibrium reaction, most commercial manufacturing methods generally require heating the reactants with an excess of the alcohol - the more volatile reactant. This helps drive the equilibrium in the direction of t,he ester product. Water of reaction is removed either by azeotrop-ing with a special agent such as xylene or by vacuum distillation and stripping. The reaction progress is followed by measuring acidity (81). The crude ester can be refined by various methods to improve quality. For example, the ester can be treated with sodium carbonate to neutralize trace acidity (9). 

History of Silica Sol Manufacturing Methods. Although numerous techniques have been proposed for manufacturing of silica sols, including dialysis (10), electrodialysis (II), peptization (12), acid neutralization (13), and ion exchange (3,14), the last three methods have come to be used most commonly. At present, the ion-exchange method is considered the most prominent technique. 

Figure 2. Flow chart of acid-neutralization method for manufacturing silica...

Acid-cataly2ed hydroxylation of naphthalene with 90% hydrogen peroxide gives either 1-naphthol or 2-naphthiol at a 98% yield, depending on the acidity of the system and the solvent used. In anhydrous hydrogen fluoride or 70% HF—30% pyridine solution at — 10 to + 20°C, 1-naphthol is the product formed in > 98% selectivity. In contrast, 2-naphthol is obtained in hydroxylation in super acid (HF—BF, HF—SbF, HF—TaF, FSO H—SbF ) solution at — 60 to — 78°C in > 98% selectivity (57). Of the three commercial methods of manufacture, the pressure hydrolysis of 1-naphthaleneamine with aqueous sulfuric acid at 180°C has been abandoned, at least in the United States. The caustic fusion of sodium 1-naphthalenesulfonate with 50 wt % aqueous sodium hydroxide at ca 290°C followed by the neutralization gives 1-naphthalenol in a ca 90% yield. 

The general manufacturing scheme for phosphate salts is shown in Figure 11. Condensed phosphates are prepared from the appropriate orthophosphate or mixture of orthophosphates, so the preparation of orthophosphates must be considered first for the manufacture of any phosphate salt. Phosphoric acid is neutralized to form a solution or slurry with a carefully adjusted acid/base ratio according to the desired orthophosphate product. The orthophosphate may be recovered either by crystallization from solution, or the entire solution or slurry may be evaporated to dryness. The dewatering (qv) method is determined by the solubihty properties of the product and by its desired physical properties such as crystal size and shape, bulk density, and surface area. Acid orthophosphate salts may be converted to condensed phosphates by thermal dehydration (calcination). 

Manufacture. Historically, ammonium nitrate was manufactured by a double decomposition method using sodium nitrate and either ammonium sulfate or ammonium chloride. Modem commercial processes, however, rely almost exclusively on the neutralization of nitric acid (qv), produced from ammonia through catalyzed oxidation, with ammonia. Manufacturers commonly use onsite ammonia although some ammonium nitrate is made from purchased ammonia. SoHd product used as fertilizer has been the predominant form produced. However, sale of ammonium nitrate as a component in urea—ammonium nitrate Hquid fertilizer has grown to where about half the ammonium nitrate produced is actually marketed as a solution. 

In the manufacture of ethylene dibromide, gaseous ethylene is brought into contact with bromine by various methods, allowing for dissipation of the heat of reaction (100—102). Eree acids are neutralized and the product maybe fractionally distilled for purification. Typical specifications call for a clear Hquid with 99.5% purity min sp gr (25/25°C), 2.170—2.180 boiling range, 130.4—132.4°C APHA color, 200 max water, 200 ppm max acidity as HCl, 0.0004 wt % max and nonvolatile matter, 0.0050 wt % max. 

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Dibromoethane is a halogenated aliphatic hydrocarbon produced when gaseous ethylene comes in contact with bromine. The mixing of ethylene and bromine is accomplished in a variety of ways. One of the more common manufacturing processes involves a liquid-phase bromination of ethylene at 35°-85°C. After the bromination of ethylene, the mixture is neutralized to free acid and then purified by distillation. Other methods of 1,2-dibromoethane formation include the hydrobromination of acetylene and a reaction of 1,2-dibromoethane with water (Fishbein 1980 HSDB 1989). 

In connection with the elaboration of specific procedures for the manufacture of both of the isosorbide mononitrates, methods were developed to shift, with high regioselectivity, the course of the acylation reaction either towards the 5 (endo) or the 2 (exo) position, depending on the conditions applied.104-106 Thus, isosorbide 5-acylates are obtained in 70-85% yield when 3 is treated with the appropriate acid anhydride in the presence of lead(II) oxide or acetate for 20 to 40 h at room temperature. To avoid transesterifications to the appropriate 2-acylate, the workup procedures, especially during the distillation, have to be conducted under strictly neutral conditions. The contrary effect, a remarkable enrichment by the isosorbide 2-acylate (up to 90%) is realized by a transesterification process mediated by a small proportion of sodium or potassium carbonate, hydroxide, or meth-oxide, which are added to the acylation mixture from isosorbide at HOMO0, and subsequent removal of the 2-acylate by vacuum distillation.104 These two regioselective acylation methods may be used for aliphatic, as well as for aromatic, carboxylic acid anhydrides. 

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