Characterization of emissions of dioxins and furans from ethylene dichloride (EDC), vinyl chloride (VCM) and polyvinylchloride (PVC) manufacturing facilities in the United States. I. Resin, treated wastewater, and ethylene dichloride

Under the auspices of its Dioxin Characterization Program, members of The Vinyl Institute (VI), have analyzed for potential polychlorinated dibenzodioxin/furan (PCDD/F) concentrations in polyvinylchloride (PVC) resins, treated wastewater effluent and ethylene dichloride (EDC) product at EDC, vinyl chloride monomer (VCM) and PVC manufacturing facilities in the U.S. and Canada. No 2,3,7,8-tetrachlorodibenzodioxin (TCDD) was detected in any sample analyzed under the program to date. Trace concentrations (low pg/g) of PCDD/F were detected in only a few samples of PVC resins and EDC product. Treated wastewater contained low ppq concentrations of PCDD/F. All concentrations are expressed as Toxic Equivalents (TEQ). Extrapolation of these data shows that the contribution of EDC/VCM/PVC manufacturing via these media constitutes substantially less than 1 percent of the estimated annual U.S. dioxin releases to the environment.     

Microscopic Visualization Technique to Predict the Permeation of Organic Solvents through PVC Pipes in Water Distribution Systems

Organic contaminants may permeate through plastic pipes in water distribution systems and adversely affect the quality of drinking water. In this study, we developed a microscopic visualization technique to investigate the permeation of common organic contaminants (benzene, toluene, ethylbenzene, xylene, and trichloroethene) through polyvinyl chloride (PVC) pipes. By observing the propagation of organic moving fronts in the pipe materials with a light microscope, the technique was able to predict the permeation breakthrough times through PVC pipes that were determined in the pipe-bottle test. The advance of an organic moving front was found to be linearly dependent on the square-root of time and the propagation rate increased with an increase in the external organic chemical activity. Permeation of organic mixtures into PVC pipes was found to be additive in proportion to the permeation rates and volume percents of each component. In combination with a 2-year pipe-bottle test for PVC pipes exposed to premium gasoline, mathematical extrapolations based on the microscopic visualization tests predicted that PVC pipe are likely to resist permeation by commercial gasoline for the service life of the pipe.     

Analysis of PVC Pipe-Wall Viscoelasticity during Water Hammer

This research work focuses on the analysis of hydraulic transients in polyvinyl chloride (PVC) pipes, which are characterized by a viscoelastic rheological behavior. Transient pressure data were collected in a pipe rig consisting of a set of PVC pipes. The creep function of the PVC pipes was determined by using an inverse transient model based on collected transient pressure data and compared with that obtained by carrying out mechanical tensile tests of PVC pipe specimens. The numerical results obtained from the transient solver have shown that the attenuation, dispersion, and shape of transient pressures were well described. The incorporation of the viscoelastic mechanical behavior in the hydraulic transient model has provided an excellent fitting between numerical results and observed data. Calibrated creep function based on inverse analysis fit the one determined by mechanical tests well, which emphasized the importance of pipe-wall viscoelasticity in hydraulic transients in PVC pipes.     

In vitro release characteristics of bioactive molecules from dextran dialdehyde cross-linked gelatin hydrogel films

Vinyl chloride monomer (VCM) is a human carcinogen. However, the exact mechanism of carcinogenesis remains unclear. VCM may be metabolized by cytochrome P450 2E1 (CYP2E1), aldehyde dehydrogenase 2 (ALDH2) and glutathione S-transferases (GSTs). Thus workers with inherited variant metabolic enzyme activities may have an altered risk of genotoxicity. This study was designed to investigate which risk factors might affect sister chromatid exchange (SCE) frequency in polyvinyl chloride (PVC) workers. Study subjects were 44 male workers from three PVC factories. Questionnaires were administered to obtain detailed histories of cigarette smoking, alcohol consumption, occupations, and medications. SCE frequency in peripheral lymphocytes was determined using a standardized method, and CYP2E1, GSTM1, GSTT1 and ALDH2 genotypes were identified by the polymerase chain reaction (PCR). Analysis revealed that smoking status and exposure to VCM were significantly associated with increased SCE frequency. The presence of ALDH2 1-2/2-2 genotypes was also significantly associated with an elevation of SCE frequency (9. 5 vs. 8.1, p<0.01). However, CYP2E1, GSTM1 or GSTT1 genotypes were not significantly associated with SCE frequency. When various genotypes were considered together, combination of CYP2E1 c1c2/c2c2 with ALDH2 1-2/2-2 showed an additive effect on SCE frequency. Similar results were also found for the combination of smoking with CYP2E1, or smoking with ALDH2. These results suggest that VCM workers with ALDH2 1-2/2-2 genotypes, who also smoke, may have increased risk of DNA damage.     

连铸冷却水复合膜过滤器技术的研发

为了钢铁工业节能减排、降低水污染和吨钢耗水量,进行了转炉炼钢连铸冷却水过滤器技术的研发,成功开发了一种以多孔PVC陶瓷复合管为过滤元件的过滤器装置。对由多孔PVC陶瓷复合管过滤器过滤的污泥进行检测,可知多孔陶瓷复合过滤管具有很好的分离效果。检测过滤前后的水质,发现过滤后水的浊度和悬浮物含量显著降低,水质达到指标要求。通过工业试验研究和近3年的实际应用,确定了多孔PVC陶瓷复合过滤设备的最佳操作条件和反冲洗条件。     

Field Studies of Discoloration in Water Distribution Systems: Model Verification and Practical Implications

Discoloration in water distribution systems has been studied in partnership with a number of U.K. water companies by measuring the turbidity response to changes in hydraulic conditions induced by systematic flushing. The resulting data was used to verify a predictive empirical model and hence the underlying assumptions made in its development. Model simulations, made using previously established parameters defined solely by pipe diameter and pipe material, are presented alongside measured data to demonstrate this verification. The primary cause of discoloration observed is the mobilization of material from cohesive layers bonded to pipe walls. These layers demonstrate a profile of increasing shear strength with increasing degree of discoloration. Differences are demonstrated in the layer and ultimate shear strength characteristics of the discoloration layers formed in iron and plastic pipes, with a modeled shear stress of 1.2?N/m2 shown to exhaust material layers in plastic pipes. Based on the observed data it is theorized that accumulation of material to the pipe walls is primarily dependent on two mechanisms; ubiquitous background concentrations in the bulk water, and if present corrosion by-products from iron pipes and fittings. A consequence of this is that all pipes within a water distribution system are susceptible to the development of material layers. In the formulation of operation and maintenance strategies it is suggested that iron and plastic pipes should be treated differently to obtain optimum operational effectiveness and minimize discoloration risk.     

Separation and recovery of potassium chloride from sinter dust of a steel plant

Many companies return sinter dust to sintering directly, resulting in circulation and accumulation of harmful elements, which will affect the collection efficiency, sinter quality, and the grade of blast furnace seriously. A new separation and recovery process of potassium from the dust was proposed, which included water leaching, solid liquid separation, purification, vacuum evaporation and cooling crystallisation. The results showed that the optimum conditions were as follows: the ratio of solid to liquid?=?1:3, leaching time?=?40?min, and leaching temperature?=?80°C, leaching rate of potassium chloride reaches 99.99%. When solution weight loss is 97.5%, the evaporation of potassium chloride product reaches 97.96%, purity of potassium chloride in the crystal can be 75.15%. Based on experiment results, a mathematical model of leaching kinetic of potassium chloride including stirring temperature and leaching ratio is proposed.     

Why must we manufacture vinyl chloride and polyvinyl chloride?

The manufacture of PVC is necessary for supplying the demands of modern society, for maintaining the equilibrium in the chemical industry such as the manufacture of caustic soda solution-chlorine by means of rocksalt electrolysis, and for the safe disposal of chlorine for environmental reasons. The manufacture of vinyl chloride and dichloroethane is illustrated. The conventional processing of PVC into consumer goods, after treatment of rigid and plasticized PVC compounds or granulate, is demonstrated.     

Combined processing technology of the Udokan sulfide copper concentrate

The combined processing variant of the Udokan sulfide copper concentrate involving low-temperature roasting with potassium chloride and the subsequent two-stage leaching of the obtained sinter consisting of copper chloride and potassium salts is described. At the first stage, water-soluble salts are leached (potassium sulfate and chloride) with water and, at the second stage, copper chloride is leached with sulfuric acid. The final products are copper vitriol and potassium fertilizer. The parameters of the main stages of the suggested technology are optimized.     

Leaching of CuFeS2 by aqueous FeCl3, HCl,and NaCl: Effects of solution composition and limited oxidant

Batch leaching experiments were performed in which the initial amounts of chalcopyrite and ferric chloride were selected to ensure that the oxidant was significantly depleted over the course of an experiment. Solution samples were analyzed for Cu(II) and Fe(III) by visible spectrophotometry and for total copper and total iron by atomic absorption, making it possible to measure changes in the solution component concentrations as leaching progressed. For selected samples, the solution potential was also measured. In all experiments, the Cu(II) concentration passed through a maximum and, simultaneously, the Cu(I) concentration increased very sharply. An acceleration in the total rate of leaching was normally observed at the same time. Early in a leach, the solution potential was too high for the reduction of Cu(II) to Cu(I) to take place at the time of the increase in the overall leaching rate, however, the solution potential dropped sharply during a span of a few hours, reaching a value low enough that reduction of cupric ion became possible. The amount of Cu(I) present at the completion of a leach was dependent on the total chloride concentration of the system. The highest Cu(I)/Cu ratios were observed in systems with the highest chloride concentrations. The ultimate extent of CuFeS₂ leaching was dependent on the initial FeCl₃ and total chloride concentrations; the FeCl₃ was virtually completely consumed and the total chloride concentration controlled the extent to which Cu(II) was reduced by reaction with chalcopyrite.     

Set Sprinkler Irrigation and Its Cost

In this study, annual water application costs per unit area (ha) have been analyzed at the level of irrigation subunit in set sprinkler irrigation systems designed with pipes of different materials. In the cost, investment (pumping, pipes, sprinklers, ditches), energy, labor, maintenance, and water costs have been considered. Four systems were studied: one with buried pipes, in a permanent solid-set system, using: (a) polyvinyl chloride with buried pipes (PVCb), and three with pipes on the surface in surface solid-set systems, using (b) polyvinyl chloride pipes, (c) polyethylene pipes, and (d) aluminum pipes. The correct selection of the irrigation subunit size and shape can lead to a significant decrease in cost. The most economic irrigation subunits, among the four systems studied, were those formed by four laterals and a number of sprinklers per lateral of 10, 9, and 6 at 12?m×12?m, 12?m×18?m, and 18?m×18?m spacing, respectively. The most influential factor on the annual water application cost was spacing. Considering total annual cost, water cost was the most important, followed by investment and energy. Among the analyzed systems, the permanent system using PVCb produced the lowest annual water application cost per unit area.     

Short-term chronoamperometric screening of chlorpromazine-package interactions

A new electroanalytical method has been developed to measure and predict solute sorption interactions with solid surfaces. By maximizing surface-to-volume ratios, this method significantly reduces the study time of drug-package interactions and allows prediction of possible long-term effects. Chronoamperometry experiments were run in 40 microL drops of solution containing drug placed on a solid substrate disk of about 7 mm diameter in a sample cell designed to accommodate a miniaturized three-electrode setup. Logarithmic current signatures obtained by computing Delta(ln i)/Delta(ln t) were used to define the experimental conditions necessary to avoid the kinetic complications of chlorpromazine oxidation in the interpretation of the results of the chronoamperometric analysis. Results of sorption studies of chlorpromazine to glass, polypropylene, high density polyethylene, poly(ethylene terephthalate), ethylene vinyl acetate, and poly(vinyl chloride) are presented. The small volume sorption experiments demonstrated that chlorpromazine interacts most quickly with PVC and HDPE and least with glass and polypropylene. Long term stability tests confirmed these predictions, thereby indicating that the small volume method makes drug-package interaction studies feasible in early development. The generation and analysis of Delta(ln i)/Delta(ln t) signature curves extends the usefulness of the electroanalytical method to other systems by accurately identifying the appropriate time domains for steady state or Cottrell behavior.     

The kinetics of dissolution of chalcopyrite in ferric ion media

The kinetics of dissolution of chalcopyrite (CuFeS₂) in ferric chloride-hydrochloric acid and in ferric sulfate-sulfuric acid solutions have been investigated using the rotating disk technique. Over the temperature range 50 to 100?C, linear kinetics were observed in the chloride media while nonlinear kinetics were noted in the sulfate system. The apparent activation energy in the chloride system was about 11 kcal/mole. The rate increased with increasing ferric chloride concentrations but was insensitive to the concentrations of hydrochloric acid, the ferrous chloride reaction product and “inert? magnesium or lithium chlorides. Cupric chloride substantially accelerated the rate. Small amounts of sulfate in an otherwise all chloride system greatly reduce the chalcopyrite leaching rate; still larger amounts of sulfate make the system behave essentially like the slower-reacting ferric sulfate medium.     

铅阳极泥氯化浸出液除氟研究

选用氯化钠脱除铅阳极泥氯化浸出液中的氟硅酸和氟硅酸盐,考察了氯化钠加入量、反应时间、沉降时间、温度等对氟脱除率的影响。在最佳工艺条件下,浸出液中氟浓度可降至2.43g/L以下,除氟率达87.7%。除氟后溶液在蒸馏过程中不产生结晶物,避免蒸馏管道发生堵塞现象,馏出液中氟浓度均在3g/L以下,可以作为稀酸返回浸出。     

Field Study to Investigate WIDE Technology for TCE Extraction

A full-scale field study was conducted using well injection depth extraction (WIDE) technology to remove trichloroethylene (TCE) from subsurface profiles with fine-grained soils. WIDE incorporates the use of geosynthetic wick drains, attached to an aboveground PVC pipe network, designed to (1) extract contaminated fluids from a specific depth using vacuum pressure, and/or (2) inject flushing solutions. Both extraction-only and concurrent injection-extraction testing schemes were conducted, and fluid flow rates, TCE recovery rates, and groundwater elevations were monitored over a 9?month time interval. During extraction-only operational schemes, gas-phase TCE extraction rates were significantly higher than liquid-phase extraction rates due to the increased volume of air within the geosynthetic wells and PVC piping. TCE extraction rates were less than 2,000?mg/h for airflow rates less than 100,000?L/h, and increased significantly to 5,700?mg/h as the airflow rate approached 600,000?L/h. Long term testing and sampling is needed to quantify system performance and determine tailing and rebounding effects in comparison to conventional methods. The behaviors and trends observed during the field study are presented and discussed.     

Metal lanolin fatty acid as novel thermal stabilizers for rigid poly（vinyl chloride）

The synergistic stabilization effect of different metal lanolin fatty acids as natural-based thermal stabilizers for poly(vinyl chloride) (PVC) including calcium lanolin fatty acid (Calan2),zinc lanolin fatty acid (Znlan2) and lanthanum lanolin fatty acid (Lalan3) were studied through Congo red testing,color measurements,FTIR analyses and thermal behavior in this paper. The results showed that Lalan3/Calan2/Znlan2 stabilizers exhibited more excellent thermal stabilization efficiency to PVC than Calan2/Znlan2 thermal stabilizers,and the optimal mass ratio of Lalan3/Calan2/Znlan2 was 8:9:3. At last,the effect of degradation mechanism on PVC and synergistic stabilization was also investigated by FTIR analyses and thermal behavior.     

Stability and compatibility of granisetron hydrochloride in i.v. solutions and oral liquids and during simulated Y-site injection with selected drugs

The stability and compatibility of granisetron hydrochloride in common i.v. fluids and oral liquids and during simulated Y-site injection with selected drugs were studied. One milliliter of solution containing granisetron 1 mg (as the hydrochloride salt) was added to 50 mL of 5% dextrose injection, 5% dextrose and 0.9% sodium chloride injection, 5% dextrose and 0.45% sodium chloride injection, or 0.9% sodium chloride injection in polyvinyl chloride (PVC) bags and to 5 mL of 5% dextrose injection, 0.9% sodium chloride injection, or bacteriostatic water for injection in polypropylene syringes and stored at room temperature (20 degrees C) for 24 hours. One milliliter of the granisetron hydrochloride injection was added to 50 mL of apple juice, orange juice, cola, or an electrolyte replacement solution and stored for 60 minutes at room temperature. Twenty-nine drugs were mixed with the granisetron hydrochloride injection in 0.9% sodium chloride injection in volumes simulating Y-site injection and stored at room temperature. Finally, dexamethasone sodium phosphate injection 0.5 mL and 1 mL of the granisetron hydrochloride injection were added to 50 mL of 0.9% sodium chloride injection in a PVC bag and stored for 60 minutes. Drug concentrations were determined by high-performance liquid chromatography, and color, clarity, and pH were evaluated. Granisetron hydrochloride was stable in and compatible with all the i.v. solutions and oral liquids. Neither granisetron nor any of the drugs it was tested with during simulated Y-site injection showed any physical changes except for a slight Tyndall effect in the granisetron hydrochloride-doxorubicin hydrochloride combination; all the drugs retained at least 96% of initial concentrations. Granisetron and dexamethasone sodium phosphate were stable and compatible in the admixture. Granisetron 1 mg (as the hydrochloride salt) was stable for 24 hours in four i.v. infusion fluids in PVC bags and in 5% dextrose injection, 0.9% sodium chloride injection, and bacteriostatic water for injection in polypropylene syringes; for 1 hour in four oral liquids; for 4 hours in the presence of each of 29 drugs during simulated Y-site injection; and for 1 hour when mixed with dexamethasone sodium phosphate in 0.9% sodium chloride injection in a PVC bag.     

Pb in Tap Water Following Simulated Partial Lead Pipe Replacements

The concentrations of total, colloidal, and truly dissolved lead (Pb) were investigated in tap water following laboratory simulations of partial lead pipe replacements. Old lead pipes were recovered from service in New Orleans, La and mounted horizontally in an experimental apparatus at Tulane Univ. Municipal water was diverted for two weeks at low flowrates of 0.2 or 1.1?L/min (0.05 or 0.3?gal/min) through two pipe trains operated continuously and two pipe trains operated intermittently. Samples were collected to determine relative concentrations and time needed for each form of Pb (total, colloidal, and truly dissolved) to stabilize below the U.S. Environmental Protection Agency action level (AL) of 15?μg/L Pb. Results demonstrate that total Pb concentrations exceeded the AL immediately following simulated partial pipe replacements. In most cases, total Pb concentrations were reduced below the AL by flushing for 15–30?min but subsequent sampling revealed total Pb concentrations greater than the AL. Continuous flow pattern flushing was more effective at stabilizing total Pb concentrations below the AL than intermittent flows. Results also demonstrate that colloidal Pb concentrations were 38–54% of total Pb and truly dissolved Pb concentrations were 41–60% of total Pb concentrations after stabilization.     

Full-scale studies of factors related to coliform regrowth in drinking water

An 18-month survey of 31 water systems in North America was conducted to determine the factors that contribute to the occurrence of coliform bacteria in drinking water. The survey included analysis of assimilable organic carbon (AOC), coliforms, disinfectant residuals, and operational parameters. Coliform bacteria were detected in 27.8% of the 2-week sampling periods and were associated with the following factors: filtration, temperature, disinfectant type and disinfectant level, AOC level, corrosion control, and operational characteristics. Four systems in the study that used unfiltered surface water accounted for 26.6% of the total number of bacterial samples collected but 64.3% (1,013 of 1,576) of the positive coliform samples. The occurrence of coliform bacteria was significantly higher when water temperatures were > 15 degrees C. For filtered systems that used free chlorine, 0.97% of 33,196 samples contained coliform bacteria, while 0.51% of 35,159 samples from chloraminated systems contained coliform bacteria. The average density of coliform bacteria was 35 times higher in free-chlorinated systems than in chloraminated water (0.60 CFU/100 ml for free-chlorinated water compared with 0.017 CFU/100 ml for chloraminated water). Systems that maintained dead-end free chlorine levels of < 0.2 mg/liter or monochloramine levels of < 0.5 mg/liter had substantially more coliform occurrences than systems that maintained higher disinfectant residuals. Free-chlorinated systems with AOC levels greater than 100 micrograms/liter had 82% more coliform-positive samples and 19 times higher coliform levels than free-chlorinated systems with average AOC levels less than 99 micrograms/liter. Systems that maintained a phosphate-based corrosion inhibitor and limited the amount of unlined cast iron pipe had fewer coliform bacteria. Several operational characteristics of the treatment process or the distribution system were also associated with increased rates of coliform occurrence. The study concludes that the occurrence of coliform bacteria within a distribution system is dependent upon a complex interaction of chemical, physical, operational, and engineering parameters. No one factor could account for all of the coliform occurrences, and one must consider all of the parameters described above in devising a solution to the regrowth problem.     

某碱性铀矿石不同去钙工艺对比试验

对碱性铀矿石进行盐酸去钙预处理,Z1柱采用池浸换液方式去钙,Z2柱采用饱水状态下连续去钙,通过调节换液频率或进液速度与盐酸酸度,使浸出液pH均保持在2左右。试验结果表明,Z2柱累计去钙率为64.8%时,去钙周期为5.38d,耗酸率(34%的浓盐酸质量/矿石质量)为11.49%;相比Z1柱,连续去钙周期缩短80%,液固比降低35%,耗酸率减少4个百分点左右。连续去钙工艺高效可行。