Oil Soap

Castile soap is manufactured from olive oil, transparent soap from decolorized fats and liquid green soap from KOH and vegetable oils. Soaps are sometimes superfatted in that they contain some free fatty acid. 

Tall oil rosin Tall oil rosin pOR) Tall oils Tall oils acids Tall-oil soaps Tallow... 

Dipropylene glycol is produced in the manufacture of propylene glycol and finds utiUty as an indirect food additive, in brake-fluid formulations, cutting oils, soaps, and solvents. Tripropylene glycol also finds use as a solvent, as textile soaps, and as lubricants (273). 

In the initial black Hquor concentration, saponified fatty and resin acid salts separate as tall oil soaps (see Tall oil). These soaps can be skimmed from the aqueous spent Hquor, acidified, and refined to give a cmde tall oil composed of resin acids, chiefly abietic and neoabietic fatty acids, chiefly oleic and Hnoleic and an unsaponifiable fraction made of phytosterols, alcohols, and hydrocarbons. Tall oil is fractionated primarily into fatty acids (see... 

A second field evaluation of the ASP process has been initiated in Wyoming. Additionally, an ASP field project has been designed for the Peoples Repubhc of China. The appHcability of the ASP process to a variety of reservoirs has yet to be fully determined. AppHcation of alkali and alkali polymer flooding has been limited to cmde oils having discernible acid numbers, wherein the alkali produced cmde oil soaps which in combination with alkali resulted in providing low interfacial tensions. The ASP process appears to be suitable for cmde oils with nil acid numbers (177), and hence should have broad apphcabdity. 

Process Sequence. The process sequence consists of recovery of tall oil soap from the pulping blackhquor, acidulation, ie, conversion of the soap into CTO with sulfuric acid, fractional distillation to separate rosin, and fatty acids and purification of the fatty acid fraction. 

Black Liquor Soap Recovery. Black Hquor soap consists of the sodium salts of the resin and fatty acids with small amounts of unsaponifiables. The soap is most easily separated from the black Hquor by skimming at an intermediate stage, when the black Hquor is evaporated to 25% soHds (7). At this soHds level, the soap rises in the skimmer at a rate of 0.76 m/h. At higher soHds concentrations, the tall oil soap is less soluble, but higher viscosity lowers the soap rise rate and increases the necessary residence times in the soap skimmer beyond 3—4 hours. The time required for soap recovery can be reduced by installing baffles, by the use of chemical flocculants (8,9), and by air injection into the suction side of the soap skimmer feed pump. Soap density is controUed by the rate of air injection. Optimum results (70% skimmer efficiency) are obtained at a soap density of 0.84 kg/L (7 lb/gal). This soap has a minimum residual black Hquor content of 15% (10—12). 

Fisch-kdmer, n.pl. Indian berries (cocculus indicus). -leim, m. fish glue, isinglass, Pharm.) ichthyocolla. -lelmgummi, n. sar-cocolla. -mehl, n. fish meal, -dl, n. fish oil ichthyol. -olselfe, /. fish oil soap, -schwanz,... 

Kali-kugel, /. potash bulb, -lauge, /. potash lye, caustic potash solution, -losung, /. potash solution, -metall, n. (metallic) potassium. -olivenolseife, /. potash olive oil soap, -praparat, n. potash (or potassium) preparation. -reibe,/. (Petro. ) potash series, -roh-salz, n. crude potassium salt, -salpeter, m. 

Kokosnuss,/. coconut, -bast, m. coconut bast, coco fiber, -fett, n. coconut oil. -milch, /. coconut milk. -81,n. coconut oil. -Slseife,/. coconut-oil soap, -talg, m. coconut oil. 

Olefinketon, n, olefinic ketone, olefin ketone, Olein-saure,/, oleic acid, -saureseife, -seife,/. olein soap, red-oil soap, -schmdlze,/, (Tea> tiles) olein softener, olein emulsion, olen, v.t. oil lubricate, grease. 

Palm-kemdl n. palm-kernel oil. -kemolselfe, -kernseife, /. palm(-kernel) oil soap, -lilie, /. yucca, -nuss, /. palm nut, palm kernel coconut. -nussSl,n. palm-kernel oil coconut oil. -ol, n. palm oil. -dlseife, /. palm oil soap, -seife, /. palm (oil) soap, -sekt, m. palm wine, palm toddy, -starke, /. palm starch, sago, -wachs, n. palm wax. -zucker, m. palm sugar, jaggery. 

Ricinus, m. castor-oil plant, -ijl, n. castor oil. -(ilsaure, /. ricinoleic acid. -Slseife, /. caator-soap, -olsulfosaure, /. castor-oil sulfonic acid, -samen, m. castor bean, -saure, /. ricinic (ricinoleic) acid, -seife, /. castor-oil soap. 

Terpentin-harz, n. turpentine resin. -81, n. (oil of) turpentine rosin oil. -fllersatz, m. turpentine substitute, -Olfimis, m. turpentine varnish, -olseife, /. turpentine-oil soap, -pech, n. turpentine pitch, -salbe, /. turpentine ointment, -spiritus, m. = Terpen-tingeist. 

Tran-leder, n. leather dressed with train oil, -schmlere, /. (Leather) daubing, -seife, /. train-oil soap,... 

Process contaminants such as black liquor or saponified organic oils (soaps). 

Non-destructive partial stripping techniques for basic dyes on acrylic fibres are carried out at 100 °C (or higher if possible) using, for example, 1-10% o.w.f. anionic retarder and 1 g/1 acetic acid (60%), or 1-5 g/1 Marseilles (olive oil) soap. Destructive stripping requires acidified (pH 5.5-6.0) sodium hypochlorite, followed by an antichlor treatment in sodium dithionite or sodium bisulphite. In some cases a preliminary boiling treatment in 5 gA monoethanolamine and 5 g/1 sodium chloride is said to improve the effect of the stripping treatment. 

Formulating an hypothesis The clogging of the centrifuge is due to iron particles mixed with coconut oil, soaps, and other normal ingredients of crude coconut oil. 

P.B1.25 is very fast in application it is fast to fats, oils, soap, and paraffin, which makes it a suitable candidate for packaging inks. Its lightfastness, however, is not excellent. In natural rubber, P.B1.25 tolerates curing very well, and it bleeds neither into the rubber nor into the fabric backing (Sec. 1.8.3.6). In rubber, the pigment is fast to cold and hot water, to soap, soda, and alkali solutions, and to acetic acid. 

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