Purification of phosphoric acid by solvent extraction

This work follows a feasibility study (187) which suggested that a process for purifying wet-process phosphoric acid by solvent extraction should be economically viable. The work was divided into two main areas, (i) chemical and physical measurements on the three-phase system, with or without impurities; (ii) process simulation and optimization. The object was to test the process technically and economically and to optimise the type of solvent. The chemical equilibria and distribution curves for the system water - phosphoric acid - solvent for the solvents n-amyl alcohol, tri-n-butyl phosphate, di-isopropyl ether and methyl isobutyl ketone have been determined. Both pure phosphoric acid and acid containing known amounts of naturally occurring impurities (Fe P0 4 , A1P0 4 , Ca3(P04)Z and Mg 3(P0 4 )Z) were examined. The hydrodynamic characteristics of the systems were also studied. The experimental results obtained for drop size distribution were compared with those obtainable from Hinze's equation (32) and it was found that they deviated by an amount related to the turbulence. A comprehensive literature survey on the purification of wet-process phosphoric acid by organic solvents has been made. The literature regarding solvent extraction fundamentals and equipment and optimization methods for the envisaged process was also reviewed. A modified form of the Kremser-Brown and Souders equation to calculate the number of contact stages was derived. The modification takes into account the special nature of phosphoric acid distribution curves in the studied systems. The process flow-sheet was developed and simulated. Powell's direct search optimization method was selected in conjunction with the linear search algorithm of Davies, Swann and Campey. The objective function was defined as the total annual manufacturing cost and the program was employed to find the optimum operating conditions for anyone of the chosen solvents. The final results demonstrated the following order of feasibility to purify wet-process acid: di-isopropyl ether, methylisobutyl ketone, n-amyl alcohol and tri-n-butyl phosphate.

Solvent extraction of phosphoric acid

This work investigated the purification of phosphoric acid using a suitable organic solvent, followed by re-extraction of the acid from the solvent using water. The work consisted of practical batch and continuous studies and the economics and design of a full scale plant, based on the experimental data. A comprehensive literature survey on the purification of wet process phosphoric acid by organic solvents is presented and the literature describing the design and operation of mixer-settlers has also been reviewed. In batch studies, the equilibrium and distribution curves for the systems water-phosphoric acid-solvent for Benzaldehyde, Cyclohexanol and Methylisobutylketone (MIBK) were determined together with hydrodynamic characteristics for both pure and impure systems. The settling time increased with acid concentration, but power input had no effect. Drop size was found to reduce with acid concentration and power input. For the continuous studies a novel horizontal mixer~settler cascade was designed, constructed and operated using pure and impure acid with MIBK as the solvent. The cascade incorporates three air turbine agitated, cylindrical 900 ml mixers, and three cylindrical 200 ml settlers with air-lift solvent interstage transfer. Mean drop size in the fully baffled mixer was correlated. Drop size distributions were log-normal and size decreased with acid concentration and power input and increased with dispersed phase hold-up. Phase inversion studies showed that the width of the ambivalent region depended upon rotor speed, hold-up and acid concentration. Settler characteristics were investigated by measuring wedge length. Distribution coefficients of impurities and acid were also investigated. The following optimum extraction conditions were found: initial acid concentration 63%, phase ratio of solvent to acid 1:1 (v/v), impeller speed recommended 900 r.p.m. In the washing step the maximum phase ratio of solvent to water was 8:1 (v/v). Work on phosphoric acid concentration involved constructing distillation equipment consisting of a 10& spherical still. A 100 T/d scale detailed process design including capital cost, operating cost and profitability was also completed. A profit model for phosphoric acid extraction was developed and maximised. Recommendations are made for both the application of the results to a practical design and for extensions of the study.

Prodrugs of antiviral phosphonates

Phosphonoformate and phosphonoacetate are effective antiviral agents, however they are charged at physiological pH and as such penetration into cells and diffusion across the blood-brain bamer is limited. In an attempt to increase the lipophilicity and improve the transport properties of these molecules, prodrugs were synthesised and their stabilities and reconversion to the parent compound subsequently investigated by the techniques of 31P nuclear magnetic resonance spectroscopy and high performance liquid Chromatography. A series of 4-substituted dibenzyl (methoxycarbonyl)phosphonates were prepared and found to be hydrolytically unstable giving predominantly the diesters, benzyl (methoxycarbonyl)phosphonates. This instability arose from the electron-withdrawing effect of the carbonyl group promoting nucleophilic attack at phosphorus. It was possible to influence the mechanism and, to some extent, the rate of hydrolysis of the phosphonoformate triesters to the diesters by varying the electronic nature of the substituent in the 4-position of the aromatic ring. Strongly electron-withdrawing groups increased the sensitivity of phosphorus to nucleophilic attack, thus promoting P-O .bond cleavage and rapid hydrolysis. Conversely, weakly electron-withdrawing substituents encouraged C-O bond fission, presumably through resonance stabilisation of the benzyl carbonium ion. The loss of the protecting group on phosphorus was in competition with nucleophilic attack at the carbonyl group, resulting in P-C bond cleavage with dibenzyl phosphite formation. The high instability and P-C bond fission make triesters unsuitable prodrug forms of phosphonoformate. A range of chemically stable triesters of phosphonoacetate were synthesised and their bioactivation investigated. Di(benzoyloxymethyl) (methoxycarbonylmethyl)phosphonates degraded to the relevant benzoyloxymethyl (methoxycarbonylmethyl)phosphonate in the presence of esterase. The enzymatic activation was restricted to the removal of only one protecting group from phosphorus, most likely due to the close proximity of the benzoyloxy ester function to the anionic charge on the diester. However, in similar systems di(4-alkanoyloxybenzyl) (methoxycarbonylmethyl)phosphonates degraded in the presence of esterase with the loss of both protecting groups on phosphorus to give the monoester, (methoxycarbonylmethyl)phosphonate, via the intermediary of the unstable 4-hydroxy benzyl esters. The methoxycarbonyl function remained intact. The rate of enzymatic hydrolysis and subsequent removal of the protecting groups on phosphorus was dependent on the nature of the alkanoyl group and was most rapid for the 4-nbutanoyloxybenzyl and 4-iso-butanoyloxybenzyl esters of phosphonoacetate. This provides a strategy for the design of a prodrug with sufficient stability in plasma to reach the central nervous system in high concentration, wherein rapid metabolism to the active drug by brain-associated enzymes occurs.

Pyrolysis of polyamide 6 under catalytic conditions and its application to reutilization of carpets

ε-caprolactam is a monomer of high value. Therefore, the chemical reutilization of polyamide 6 containing carpets for ε-caprolactam recovery offers some economic benefit and is performed on a technical scale with the help of the Zimmer-process. By this process polyamide 6 is depolymerized with steam and phosphoric acid. An alternative to this process is the thermal depolymerization - catalyzed or non-catalyzed. To investigate this alternative in more detail, the formal kinetic parameters of (i) the thermal depolymerization of polyamide 6, (ii) the thermal depolymerization in presence of sodium/potassium hydoxide, and (iii) the thermal depolymerization in presence of phosphoric acid are determined in this work. Based on the kinetics of the catalyzed or non-catalyzed depolymerization a stepwise pyrolysis procedure is designed by which the formation of ε-caprolactam from polyamide 6 can be separated from the formation of other pyrolysis products. © 2001 Elsevier Science B.V.

Erythrocyte antioxidant protection of rose hips (Rosa spp.)

Rose hips are popular in health promoting products as the fruits contain high content of bioactive compounds. The aim of this study was to investigate whether health benefits are attributable to ascorbic acid, phenols, or other rose-hip-derived compounds. Freeze-dried powder of rose hips was preextracted with metaphosphoric acid and the sample was then sequentially eluted on a C18 column. The degree of amelioration of oxidative damage was determined in an erythrocyte in vitro bioassay by comparing the effects of a reducing agent on erythrocytes alone or on erythrocytes pretreated with berry extracts. The maximum protection against oxidative stress, 59.4 ± 4.0% (mean standard deviation), was achieved when incubating the cells with the first eluted meta-phosphoric extract. Removal of ascorbic acid from this extract increased the protection against oxidative stress to 67.9 ± 1.9% . The protection from the 20% and 100% methanol extracts was 20.8 ± 8.2% and 5.0 ± 3.2% , respectively. Antioxidant uptake was confirmed by measurement of catechin by HPLC-ESI-MS in the 20% methanol extract. The fact that all sequentially eluted extracts studied contributed to protective effects on the erythrocytes indicates that rose hips contain a promising level of clinically relevant antioxidant protection. © Copyright 2012 C. Widén et al.