Acids fatty, in soaps

Determination of the composition of different oils and fats is a very common application of the GC analysis of fatty acids. The samples under analysis are usually hydrolysed first and free fatty acids are esterified. Kleiman et al. [138] used the methanol—BF3 method for determining acyl groups in oils. Barnes and Holaday [139] started directly with ground peanuts when analysing the composition of their fats. After hydrolysis for 8 min by heating at 80°C with a methanolic solution of NaOH they carried out the esterification with 10% of methanol—BF3 at 95°C for 5 min. n-Propyl esters were utilized for the analysis of fatty acids in soaps [140]. After evolving fatty acids with the aid of orthophosphoric acid, the esters were prepared by heating with /7-propanol at 90°C for 2 min. 

The incorporation of C16-C18 and C12-C14 fatty acids in soaps is important as they provide the cleaning, solubility, and foaming properties required. Tallow and coconut oil have been the traditional sources of these fatty acids. A comparison between the fatty acid composihons of palm oh, pahn stearin, tallow, palm kernel oil, palm kernel oleins, and coconut oil (Table 41) indicates that the first three are rich in C16-C18 fatty acids while pahn kernel and coconut oils are rich in C12-C14 fatty acids. However, for pahn products to establish a niche in the market as raw materials, soap manufacturers have to be convinced that apart from price competitiveness, they will yield soaps with properties and performance comparable if not superior to those from tallow and coconut oil. 

SNG Substitute natural gas. soaps Sodium and potassium salts of fatty acids, particularly stearic, palmitic and oleic acids. Animal and vegetable oils and fats, from which soaps are prepared, consist essentially of the glyceryl esters of these acids. In soap manufacture the oil or fat is heated with dilute NaOH (less frequently KOH) solution in large vats. When hydrolysis is complete the soap is salted out , or precipitated from solution by addition of NaCl. The soap is then treated, as required, with perfumes, etc. and made into tablets. 

Methyl group (Section 2 7) The group —CH3 Mevalonic acid (Section 26 10) An intermediate in the biosyn thesis of steroids from acetyl coenzyme A Micelle (Section 19 5) A sphencal aggregate of species such as carboxylate salts of fatty acids that contain a lipophilic end and a hydrophilic end Micelles containing 50-100 car boxylate salts of fatty acids are soaps Michael addition (Sections 18 13 and 21 9) The conjugate ad dition of a carbanion (usually an enolate) to an a 3 unsatu rated carbonyl compound... 

Release agents function by either lessening intermolecular interactions between the two surfaces in contact or preventing such close contact. Thus, they can be low surface-tension materials based on aUphatic hydrocarbon, fluorocarbon groups, or particulate soHds. The principal categories of material used are waxes, fatty acid metal soaps, other long-chain alkyl derivatives, polymers, and fluorinated compounds. 

In the presence of excess fatty acid, different soap crystalline phase compounds can form, commonly referred to as acid—soaps. Acid—soap crystals are composed of stoichiometric amounts of soap and fatty acid and associate in similar bilayer stmctures as pure soap crystals. There are a number of different documented acid—soap crystals. The existence of crystals of the composition 2 acid—1 soap, 1 acid—1 soap, and 1 acid—2 soap has been reported (13). The presence of the acid—soaps can also have a dramatic impact on the physical and performance properties of the finished soap. The presence of acid—soaps increases the plasticity of the soap during processing and decreases product firmness, potentially to the point of stickiness during processing. Furthermore, the presence of the acid—soap changes the character of the lather, decreasing the bubble size and subsequently increasing lather stabiUty and... 

Sulfated Acids, Amides, and Esters. Reaction with sulfuric acid may be carried out on fatty acids, alkanolamides, and short-chain esters of fatty acids. The disodium salt of sulfated oleic acid is a textile additive and an effective lime soap dispersant. A typical sulfated alkanolamide stmcture is CiiH23C0NHCH2CH20S03Na. Others include the sulfates of mono and diethanolamides of fatty acids in the detergent range. The presence of... 

The catalytic oxidation of long-chain paraffins (C18-C30) over manganese salts produces a mixture of fatty acids with different chain lengths. Temperature and pressure ranges of 105-120°C and 15-60 atmospheres are used. About 60 wt% yield of fatty acids in the range of C12-C14 is obtained. These acids are used for making soaps. The main source for fatty acids for soap manufacture, however, is the hydrolysis of fats and oils (a nonpetroleum source). Oxidation of paraffins to fatty acids may be illustrated as ... 

Dibasic salts of dicyclopentadiene dicarboxylic acid are claimed to be active as corrosion inhibitors [444], Certain salts of fatty acids (metal soaps), together with benzotriazole, are claimed to give synergistic effects for corrosion in antifreeze-agent formulations [446]. 

Aid in the uniform dispersion of additives. Make powdered solids (e.g. particulate fillers with high energy and hydrophilic surface) more compatible with polymers by coating their surfaces with an adsorbed layer of surfactant in the form of a dispersant. Surface coating reduces the surface energy of fillers, reduces polymer/filler interaction and assists dispersion. Filler coatings increase compound cost. Fatty acids, metal soaps, waxes and fatty alcohols are used as dispersants commonly in concentrations from 2 to 5 wt %. 

Saturated hydrocarbons (waxes), fatty acids, metal soaps, fatty acid amides and esters (primarily Cig-Cis) act as internal lubricants, fluoro elastomers as external lubricants. Many other polymer additives, e.g. antistatic agents, antifogs, antioxidants, UV stabilisers, etc., act as lubricants in the barrel of the extruder once they are in the liquid form. 

In principle, the iterative experimental approach one would take today is no different than the one pursued by the product developers at Lever Brothers Co. in the early 1950 s, though possibly accumulated data about surfactants, fatty acids, and soaps in the public domain might make ingredient selection some-... 

Applying Concepts The reaction between a triglyceride and a strong base such as sodium hydroxide is called saponification. In this reaction, the ester bonds in the triglyceride are hydrolyzed by the base. The sodium salts of the fatty acids, called soaps, precipitate out, and glycerol is left in solution. 

Gibbs, F.S. The removal of fatty acids and soaps from soap manufacturing wastewaters. Proceedings of the 5th Industrial Waste Conference, Purdue University, Lafayette, IN, 1949, Vol. 5, p. 400. Greek, B.F. Detergent industry ponders products for new decade. Chem. Eng. News 1990, Jan. 29, 37-60. 

The emulsion was then allowed to separate and it was found on analysis of the soap content of the aqueous lower layer and the concentrated emulsion in the upper layer that the emulsion had abstracted soap from the solution. Owing to the fact that the fatty acids are soluble in the oil the hydrolysis of the soaps and the subsequent removal of the fatty acid in the oil phase had to be eliminated by the addition of caustic soda. In this way the true quantity of soap at the oil-water interface could be determined. Some of the results, obtained are tabulated below. 

Dampproofing admixtures are water-repelling materials such as wax emulsions, soaps and fatty acids which react with cement hydrates [84, 85]. The most widely used water-repelling materials are the calcium or ammonium salts of fatty acids such as stearates. Proprietary products are available both as dry powders and liquids. Usually, a stearate soap is blended with talc or fine silica sand and used at the prescribed dosage per weight or bag of cement. In commercial liquid preparations, the fatty-acid salt (soap) content is usually 20% or less, the balance of the solid material is made up of lime or CaCl2. Some proprietary admixtures combine two or more admixtures, e. 

Black oil should be a pure petroleum product free from fatty oils, fatty acids, resins, soaps, or other nonhydrocarbons. Sediment and sludge, insoluble in paraffin naphtha, should not exceed 12% when determined by the methods of the American Association of State Highway Officials. The product should be a distilled or fractionated oil, and should contain no oil-well water or residue therefrom. The product should be free of or contain no more than traces of naphthenic acids, naphthenes, mercaptans, soluble sulfide, and volatile sulfur derivatives. The oil should flow freely from the tank car at temperatures above 32 F. 

Molecular Association in Fatty Acid-Potassium Soap Systems... 

The composition data obtained for the series of mixed fatty acid-potassium soap systems, prepared by both the ethanol and petroleum ether routes, lend strong support to the formation of 1 to 1 acid-soap complexes. It is of interest to inquire into the phase relationships in these two-component systems. A phase diagram presented by McBain and Field (15) for the lauric acid-potassium laurate system shows that compound formation takes place between the two components at the 1 to 1 molar ratio, but the compound undergoes melting with decomposition at 91.3 °C. [A similar type of phase behavior has been reported by us for the sodium alkyl sulfate-alkyl alcohol (9) and sodium alkyl sulfonate-alkyl alcohol (12) systems, but in these cases the stoichiometry is 2 to 1]. 

Nor are those in phase 2 free of 5.8- to 5.9-micron absorbing material. The latter peak is characteristic of both free fatty acid and phase 1 acid-soap. Hence, this does not allow a definitive statement of the second species present. It is, however, likely to be phase 1 (or 3) material since the DTA results point to the absence of free fatty acid in most cases. Furthermore, acid-soap in one phase can transform to another phase as has been clearly demonstrated. 

---