Ethylene glycol/hydrocarbon system

For ethylene glycol/hydrocarbon and amine/hydrocarbon systems, the calculahon should be checked for interface flow. The allowable interface flow for these two systems is 100 m /(m -day). 

Liquid Third Phase. A third Hquid with coUoidal stmcture has been a known component in emulsions since the 1970s (22) for nonionic surfactants of the poly(ethylene glycol) alkylaryl ether type. It allows low energy emulsification (23) using the strong temperature dependence of the coUoidal association stmctures in the water—surfactant—hydrocarbon systems. 

Fig. 11. In a system of water and hydrocarbon a nonionic emulsifier with a poly(ethylene glycol) chain as the polar part dissolves in the aqueous phase at low temperatures (a) and in the oil phase at high temperatures (c). At an intermediate temperature (b) three isotropic Hquid phases may be found.

Membrane Pervaporation Since 1987, membrane pei vapora-tion has become widely accepted in the CPI as an effective means of separation and recovery of liquid-phase process streams. It is most commonly used to dehydrate hquid hydrocarbons to yield a high-purity ethanol, isopropanol, and ethylene glycol product. The method basically consists of a selec tively-permeable membrane layer separating a liquid feed stream and a gas phase permeate stream as shown in Fig. 25-19. The permeation rate and selectivity is governed bv the physicochemical composition of the membrane. Pei vaporation differs From reverse osmosis systems in that the permeate rate is not a function of osmotic pressure, since the permeate is maintained at saturation pressure (Ref. 24). 

In spite of the potentialities of reversed micelles entrapping nonaqueous highly polar solvents [34], very few investigations on the solubilization in such systems are reported in the literature. An example is the study of the solubilization of zinc-tetraphenylporphyrin (ZnTPP) in ethylene glycol/AOT/hydrocarbon systems by steady-state and transient... 

In the gas-cleaning loop, a catalyst bed system for the removal of hydrocarbons and a molecular sieve dryer for removing moisture is generally preferred to an ethylene glycol scrubber. 

DNPH-steroids can be separated by HPLC with several partition systems [31,32] including 1 % /3,/3 -oxydipropionitrile (BOP) on Zipax with eluting solvents containing 0-20% tetrahydrofuran in heptane or 2-methylheptane, or 1% ethylene glycol on Zipax with 3% chloroform in heptane as the mobile phase. Reversed-phase chromatography with 1.0% hydrocarbon polymer (HCP) or 1% cyanoethyl silicone (ANH) on Zipax and methanol-water as the mobile phase can be useful for the separation of several polar steroids. Gradient elution (water to methanol) on octadecylsilane (ODS), Permaphase (chemically bonded on Zipax), also provides a separation of polar DNPH-steroids. The separation of five DNPH-steroids on 1.5% BOP coated on Zipax is shown in Fig.4.13. 

Many ATPS systems contain a polymer which is sugar based and a second one which is of hydrocarbon ether type. Sugar-based polymers include dextran (Dx), hydroxy propyl dextran (HPDx), FicoU (Fi) (a polysaccharide), methyl cellulose (MC), or ethylhydroxyethyl cellulose (EHEC). Hydrocarbon ether-type polymers include poly (ethylene glycol) (PEG), poly (propylene glycol) (PPG), or the copolymer of PEG and PPG. De-rivatized polymers can also be useful, such as PEG-fatty acids or di-ethylaminoethyl-dextran (Dx-DEAE). 

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