Removal Of Ethylenediaminetetraacetic Acid Research Articles

Simultaneous electrochemical removal of copper and chemical oxygen demand using a packed-bed electrode cell

Copper ions and chelating agents in water were treated simultaneously by using a packed-bed electrode cell. The cathode packings were graphite particles or graphite felt; the anode packings were platinum-plated titanium pellets, β-PbO2 particles or oxidized lead spheres. The catholyte contained ethylenediaminetetraacetic acid (EDTA), nitrilotriacetic acid (NTA), iminodiacetic acid (IDA) or glycine chelate of copper, while the anolyte contained the corresponding chelating agents. The initial concentration of chelating agents was 0.01 M in each experiment. The electrowinning of copper and the removal of chemical oxygen demand (COD) were achieved in the cathodic and the anodic chamber, respectively, under galvanostatic conditions. The COD was determined by the standard KMnO4 method. Of the cathodic packings, the graphite felt gave better results than the graphite particles because of the large surface area of the felt. Of the anodic packings, the platinum-plated titanium pellets and the β-PbO2 particles showed equal suitability for COD removal. In the case of the platinum-plated titanium pellets, the current efficiency for COD removal of EDTA, NTA and IDA was 1.4, 0.7 and 0.32, respectively, in the range 0–12 kC. The removal of COD for EDTA, NTA and IDA under the same conditions was 41, 36 and 25%, respectively. In the lower pH range the electro-oxidation of EDTA proceeded more efficiently.

Regulation of the Neurospora crassa assimilatory nitrate reductase.

Reduced nicotinamide adenine dinucleotide phosphate (NADPH)-nitrate reductase from Neurospora crassa was purified and found to be stimulated by certain amino acids, citrate, and ethylenediaminetetraacetic acid (EDTA). Stimulation by citrate and the amino acids was dependent upon the prior removal of EDTA from the enzyme preparations, since low quantities of EDTA resulted in maximal stimulation. Removal of EDTA from enzyme preparations by dialysis against Chelex-containing buffer resulted in a loss of nitrate reductase activity. Addition of alanine, arginine, glycine, glutamine, glutamate, histidine, tryptophan, and citrate restored and stimulated nitrate reductase activity from 29- to 46-fold. The amino acids tested altered the Km of NADPH-nitrate reductase for NADPH but did not significantly change that for nitrate. The Km of nitrate reductase for NADPH increased with increasing concentrations of histidine but decreased with increasing concentrations of glutamine. Amino acid modulation of NADPH-nitrate reductase activity is discussed in relation to the conservation of energy (NADPH) by Neurospora when nitrate is the nitrogen source.

Steamflood Heater Scale and Corrosion

Field studies to evaluate scale and corrosion in steamflood heater tubes indicate that series-softened sodium ion-exchange water (0.5 ppm total hardness as CaCO3), containing less than 0.2 ppm iron, causes very little deposition and few tube failures. Caustic treatment reduces iron dissolved from bare soft-water distribution lines and iron scale deposition in heater tubes. Introduction When Shell Oil Co. began commercial steamflooding, the water-treating program consisted of catalyzed sodium sulfite, to remove dissolved oxygen, and conventional sodium ion-exchange softening, followed by chelation of hardness leakage with ethylenediaminetetraacetic acid (EDTA). Within 8 months the once-through steam generators (field heaters) began to experience leaks from internal thinning of the 3-in., 180 degrees return beads. Iron material balance calculations revealed a correlation between excess EDTA and iron removal rate, as shown in Fig. 1. Laboratory studies by P. J. Raifsnider, Shell Development Co., determined the leaks were most likely caused by erosion-corrosion in the presence of EDTA. Fig. 2 summarizes Raifsnider's presence of EDTA. Fig. 2 summarizes Raifsnider's experiments using carbon steel coupons in a stirred autoclave. The high concentration of EDTA used in these studies was employed to obtain a measurable effect of the treatment.Laboratory and field tests seeking alternate water-softening schemes demonstrated that series sodium ion-exchange produced water of zero hardness to the standard EDTA analytical test method. Actually, this water contained about 0.4 ppm total hardness using more sophisticated analytical techniques. Accordingly, Shell later added a second stage softener in their steamflood projects. It was noted that on cessation of EDTA treatment the iron material balance calculations began to show small amounts of iron deposition in the heater. Small deposits of calcium and magnesium compounds were also indicated.Within a year another type of tube failure manifested itself. This failure occurred in the body of the tube and consisted of slight swelling and, finally, longitudinal splitting. Analyses of scale samples from two failures and two imminent failures are shown in Tables 1 and 2, respectively. The scale in the swollen but unfailed tubes was less than 1 mm in thickness. Problem Problem The problem was tube failure because of water-side scale deposits. The purpose of this study was to determine the concentration of scale-forming ions required to form deposits. Our data indicate that the concentration of calcium, magnesium, and iron should be kept as near zero as possible to minimize scale formation. Research The source of calcium, magnesium, sodium, and silica was obviously the heater feedwater. However, the major constituent, iron, could have been from tube corrosion or iron picked up by the feedwater from steel distribution piping between the softening plant and heaters. The latter was suspected to be the most important. The power-generating industry has experienced a similar problem with boiler tube failures caused by scales found to be predominantly iron oxides. JPT P. 171