Advanced Oxidation Processes for the Removal of Antibiotics from Water
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Ozonedisinfection.Pdf
ETI - Environmental Technology Initiative Project funded by the U.S. Environmental Protection Agency under Assistance Agreement No. CX824652 What is disinfection? Human exposure to wastewater discharged into the environment has increased in the last 15 to 20 years with the rise in population and the greater demand for water resources for recreation and other purposes. Disinfection of wastewater is done to prevent infectious diseases from being spread and to ensure that water is safe for human contact and the environment. There is no perfect disinfectant. However, there are certain characteristics to look for when choosing the most suitable disinfectant: • Ability to penetrate and destroy infectious agents under normal operating conditions; • Lack of characteristics that could be harmful to people and the environment; • Safe and easy handling, shipping, and storage; • Absence of toxic residuals, such as cancer-causing compounds, after disinfection; and • Affordable capital and operation and maintenance (O&M) costs. What is ozone disinfection? One common method of disinfecting wastewater is ozonation (also known as ozone disinfection). Ozone is an unstable gas that can destroy bacteria and viruses. It is formed when oxygen molecules (O2) collide with oxygen atoms to produce ozone (O3). Ozone is generated by an electrical discharge through dry air or pure oxygen and is generated onsite because it decomposes to elemental oxygen in a short amount of time. After generation, ozone is fed into a down-flow contact chamber containing the wastewater to be disinfected. From the bottom of the contact chamber, ozone is diffused into fine bubbles that mix with the downward flowing wastewater. See Figure 1 on page 2 for a schematic of the ozonation process. -
Depa1'tment of Physical Chemistry Isl'ael
.. ANNUAL PROGRESS REPORT C00-3221-67 (For the period September 79 - July 80) Under Contract No. DOE/EV/03221 on THE NATURE OF OXYGEN CONTAINING RADICALS IN RADIATION CHEMISTRY AND PHOTOCHEMISTRY OF AQUEOUS SOLUTIONS Submitted by PROFESSOR GIDON CZAPSKI Depa1'tment of Physical Chemistry The Hebl'eW Univel'sity~ Jerusalem~ Isl'ael IJISTRIBUTIOJI OF THIS DOCUMENT IS UNUMITEJJ DISCLAIMER This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency Thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof. DISCLAIMER Portions of this document may be illegible in electronic image products. Images are produced from the best available original document. ANNUAL PROGRESS REPORT C00-3221-67 (For the period September 79 - July 80) Und~r Contract No. DOE/EV/03221·· on THE NATURE OF OXYGEN CONTAINING RADICALS IN RADIATION CHEMISTRY AND PHOTOCHEMISTRY OF AQUEOUS SOLUTIONS Submitted by PROFESSOR GIDON CZAPSKI lh~s book was ~repared as an account of work sponsored by an agency of the United States Government :!:~; the ~~•ted Stat~ ~nment nor any agency thereof, nor any of their employees, makes an~ v. -
Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates Under Reducing Environments of N2 and CO2
energies Article Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N2 and CO2 Tahereh Jalalabadi, Behdad Moghtaderi and Jessica Allen * School of Chemical Engineering, University of Newcastle, Callaghan, NSW 2308, Australia; [email protected] (T.J.); [email protected] (B.M.) * Correspondence: [email protected]; Tel.: +612-40-339-359 Received: 15 September 2020; Accepted: 12 October 2020; Published: 15 October 2020 Abstract: The impact of N2 and CO2 atmospheres on the interaction between Eucalyptus pilularis biomass and a ternary molten carbonate eutectic (Li2CO3: Na2CO3:K2CO3) has been investigated at 600 ◦C and 900 ◦C. For lower temperature conversion under CO2, prevention of volatile release in the eutectic treated biomass is slightly higher than under N2 injection; however, similar bubble-shaped morphology of the remnant char is observed under both carrier gases. By increasing the temperature to 900 ◦C under CO2, the reverse Boudouard reaction begins to consume carbon fuel, while molten carbonate gasification also accelerates the reaction to a lower temperature set point (shifted from ~735 ◦C to ~640 ◦C). The mass loss of carbonate under CO2 and N2 at 900 ◦C is 0 (negligible) and 18 wt.%, respectively. In the absence of carbon particles, the decomposition of carbonate to M2O (l) and CO2 (g), as well as molten salt vaporization, are the sole potential routes of weight loss in an inert gas. Previous observations of biomass and eutectic mixture thermochemical conversion under N2 have suggested carbon/carbonate gasification is dominant at elevated temperatures, with production of CO expected. -
The Decomposition Kinetics of Peracetic Acid and Hydrogen Peroxide in Municipal Wastewaters
Disinfection Forum No 10, October 2015 The Decomposition Kinetics of Peracetic Acid and Hydrogen Peroxide in Municipal Wastewaters INTRODUCTION Efficient control of microbial populations in municipal wastewater using peracetic acid (PAA) requires an understanding of the PAA decomposition kinetics. This knowledge is critical to ensure the proper dosing of PAA needed to achieve an adequate concentration within the contact time of the disinfection chamber. In addition, the impact of PAA on the environment, post-discharge into the receiving water body, also is dependent upon the longevity of the PAA in the environment, before decomposing to acetic acid, oxygen and water. As a result, the decomposition kinetics of PAA may have a significant impact on aquatic and environmental toxicity. PAA is not manufactured as a pure compound. The solution exists as an equilibrium mixture of PAA, hydrogen peroxide, acetic acid, and water: ↔ + + Acetic Acid Hydrogen Peroxide Peracetic Acid Water PeroxyChem’s VigorOx® WWT II Wastewater Disinfection Technology contains 15% peracetic acid by weight and 23% hydrogen peroxide as delivered. Although hydrogen peroxide is present in the formulation, peracetic acid is considered to be the active component for disinfection1 in wastewater. There have been several published studies investigating the decomposition kinetics of PAA in different water matrices, including municipal wastewater2-7. Yuan7 states that PAA may be consumed in the following three competitive reactions: 1. Spontaneous decomposition 2 CH3CO3H à 2 CH3CO2H + O2 Eq (1) 2. Hydrolysis CH3CO3H + H2O à CH3CO2H + H2O2 Eq (2) 3. Transition metal catalyzed decomposition + CH3CO3H + M à CH3CO2H + O2 + other products Eq (3) At neutral pH’s, both peracetic acid and hydrogen peroxide can be rapidly consumed by these reactions7 (hydrogen peroxide will decompose to water and oxygen via 2H2O2 à 2H2O + O2). -
University of Groningen Discovery of a Eugenol Oxidase From
University of Groningen Discovery of a eugenol oxidase from Rhodococcus sp strain RHA1 Jin, J.F.; Mazon, H.; van den Heuvel, R.H.H.; Janssen, D.B.; Fraaije, M.W. Published in: Febs Journal DOI: 10.1111/j.1742-4658.2007.05767.x IMPORTANT NOTE: You are advised to consult the publisher's version (publisher's PDF) if you wish to cite from it. Please check the document version below. Document Version Publisher's PDF, also known as Version of record Publication date: 2007 Link to publication in University of Groningen/UMCG research database Citation for published version (APA): Jin, J. F., Mazon, H., van den Heuvel, R. H. H., Janssen, D. B., & Fraaije, M. W. (2007). Discovery of a eugenol oxidase from Rhodococcus sp strain RHA1. Febs Journal, 274(9), 2311 - 2321. https://doi.org/10.1111/j.1742-4658.2007.05767.x Copyright Other than for strictly personal use, it is not permitted to download or to forward/distribute the text or part of it without the consent of the author(s) and/or copyright holder(s), unless the work is under an open content license (like Creative Commons). Take-down policy If you believe that this document breaches copyright please contact us providing details, and we will remove access to the work immediately and investigate your claim. Downloaded from the University of Groningen/UMCG research database (Pure): http://www.rug.nl/research/portal. For technical reasons the number of authors shown on this cover page is limited to 10 maximum. Download date: 23-09-2021 Discovery of a eugenol oxidase from Rhodococcus sp. -
Elementary Iodine-Doped Activated Carbon As an Oxidizing Agent for the Treatment of Arsenic-Enriched Drinking Water
water Article Elementary Iodine-Doped Activated Carbon as an Oxidizing Agent for the Treatment of Arsenic-Enriched Drinking Water Fabio Spaziani 1,2,*, Yuli Natori 1, Yoshiaki Kinase 1, Tomohiko Kawakami 1 and Katsuyoshi Tatenuma 1 1 KAKEN Inc., Mito Institute 1044 Hori, Mito, Ibaraki 310-0903, Japan 2 ENEA Casaccia, Via Anguillarese 301, 00123 Roma, Italy * Correspondence: [email protected] Received: 18 July 2019; Accepted: 23 August 2019; Published: 27 August 2019 Abstract: An activated carbon impregnated with elementary iodine (I2), named IodAC, characterized by oxidation capability, was developed and applied to oxidize arsenite, As(III), to arsenate, As(V), in arsenic-rich waters. Batch and column experiments were conducted to test the oxidation ability of the material. Comparisons with the oxidizing agents usually used in arsenic treatment systems were also conducted. In addition, the material has been tested coupled with an iron-based arsenic sorbent, in order to verify its suitability for the dearsenication of drinking waters. IodAC exhibited a high and lasting oxidation potential, since the column tests executed on water spiked with 50 mg/L of arsenic (100% arsenite) showed that 1 cc of IodAC (30 wt% I2) can oxidize about 25 mg of As(III) (0.33 mmol) before showing a dwindling in the oxidation ability. Moreover, an improvement of the arsenic sorption capability of the tested sorbent was also proved. The results confirmed that IodAC is suitable for implementation in water dearsenication plants, in place of the commonly used oxidizing agents, such as sodium hypochlorite or potassium permanganate, and in association with arsenic sorbents. -
Synthesis and Exploratory Deposition Studies of Isotetrasilane and Reactive Intermediates for Epitaxial Silicon
This is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes. Article Cite This: Inorg. Chem. 2019, 58, 3050−3057 pubs.acs.org/IC Synthesis and Exploratory Deposition Studies of Isotetrasilane and Reactive Intermediates for Epitaxial Silicon ,† † † † ‡ Barry Arkles,* Youlin Pan, Fernando Jove, Jonathan Goff, and Alain Kaloyeros † Gelest Inc., Morrisville, Pennsylvania 19067, United States ‡ SUNY Polytechnic Institute, Albany, New York 12203, United States ABSTRACT: A synthetic method is presented for the production of isotetrasilane, a higher order perhydridosilane, with the purity and volume necessary for use in extensive studies of the chemical vapor deposition (CVD) of epitaxial silicon (e-Si) thin films. The chemical characteristics, thermodynamic properties, and epitaxial film growth of isotetrasilane are compared with those of other perhydridosi- lanes. A film-growth mechanism distinct from linear perhy- ≤ dridosilanes H(SiH2)nH, where n 4, is reported. Preliminary findings are summarized for CVD of both unstrained e-Si and strained e-Si doped with germanium (Ge) and carbon (C) employing isotetrasilane as the source precursor at temper- atures of 500−550 °C. The results suggest that bis- (trihydridosilyl)silylene is the likely deposition intermediate under processing conditions in which gas-phase depletion reactions are not observed. ■ INTRODUCTION such as trisilane. However, the latter was observed to generate As emerging integrated chip (IC) and solar cell technologies gas-phase particles (silicon hydride clusters) due to its much continue to reduce individual device feature sizes, chemical higher reactivity and lower dissociation energy in comparison 5 vapor deposition (CVD) of epitaxial silicon (e-Si) has emerged to silane and disilane. -
A Study of Organosilicon Free Radicals Jay Stephen Curtice Iowa State College
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1954 A study of organosilicon free radicals Jay Stephen Curtice Iowa State College Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Organic Chemistry Commons, and the Physical Chemistry Commons Recommended Citation Curtice, Jay Stephen, "A study of organosilicon free radicals " (1954). Retrospective Theses and Dissertations. 13411. https://lib.dr.iastate.edu/rtd/13411 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. A STUDY OF ORGANOSILICON FREE RADICALS by Jay Stephen Curtice A Dissertation Sul»nitted to the Graduate Faculty in Partial Fulfillment of The Requirements for the Degree of DOCTOR OF PHILOSOPHY Major Subject: Physical Organic Chemistry Approved; Signature was redacted for privacy. Signature was redacted for privacy. In CJiiarge of Major Work Signature was redacted for privacy. Head of Major DepartMnt Signature was redacted for privacy. Dean of Graduate College Iowa State College 195^ UMI Number: DP12662 INFORMATION TO USERS The quality of this reproduction is dependent upon the quality of the copy submitted. Broken or indistinct print, colored or poor quality illustrations and photographs, print bleed-through, substandard margins, and improper alignment can adversely affect reproduction. In the unlikely event that the author did not send a complete manuscript and there are missing pages, these will be noted. -
Comparative Study of Oxidants in Removal of Chemical Oxygen Demand from the Wastewater (IJIRST/ Volume 4 / Issue 1/ 011)
IJIRST –International Journal for Innovative Research in Science & Technology| Volume 4 | Issue 1 | June 2017 ISSN (online): 2349-6010 Comparative Study of Oxidants in Removal of Chemical Oxygen Demand from the Wastewater Prof Dr K N Sheth Kavita V Italia Director PG Student Geetanjali Institute of Technical Studies, Udaipur Department of Environmental Engineering Institute of Science & Technology for Advanced Studies & Research, Vallabh Vidyanagar Abstract Chemical Oxygen Demand (COD) test involves chemical oxidation using chromic acid as a strong oxidizer. COD of a wastewater sample is the amount of oxidant- potassium dichromate that reacts with the sample when it is heated for 2 hours under controlled environmental conditions and result is expressed as mg of oxidant consumed per liter of a given sample of wastewater. COD can be helpful in determining the quantity required for dilution needed for conducting Biochemical Oxygen Demand (BOD) five day test. In the present investigation attempts have been made to use other oxidants like hydrogen peroxide H2O2, sodium hypo-chlorite, calcium hypo-chlorite and potassium permanganate for measurement of COD by standard method and compare the results obtained using potassium dichromate as strong oxidant. Experiments were carried out for each oxidizing agent for COD removal at temperatures like 1000C, 750C and 500C. The duration of exposure time in each experimental set up was taken as temperature wise, for 1000C, it was 1-5 minutes , for 750C it was 20-40 minutes and for 500C it was 45-75 minutes. It was found that temperature plays very important role in in deciding the exposure time to be allocated for reduction of COD. -
Screening 36 Veterinary Drugs in Animal Origin Food by LC/MS/MS Combined with Modified Quechers Method
Screening 36 Veterinary Drugs in Animal Origin Food by LC/MS/MS Combined with Modified QuEChERS Method Application Note Food Testing and Agriculture Authors Abstract Jin-Lan Sun, Chang Liu, Yue Song This application note introduces a modified QuEChERS method that screens food for Agilent Technologies Co., Ltd., four classes of veterinary drugs-sulfanilamides, macrocyclic lactones, quinolones, and Shanghai, 200131 China clopidols. The modified QuEChERS consists of an extraction kit (4 g Na2SO4+ Jian-Zhong Li 1 g NaCl) and a dispersive-SPE kit (50 mg PSA, 150 mg, C18EC, 900 mg Na2SO4); the Agilent Technologies Co., Ltd., extraction solvent is 1% acetic acid in acetonitrile. Satisfactory recoveries were Beijing, 100102 China achieved by this method for all four classes of veterinary drugs. The veterinary drugs were quantified by LC/ESI/MS/MS using Dynamic Multiple Reaction Monitoring (DMRM). The observed limits of detection are in accordance with the various MRLs for the four classes of veterinary drugs, and the average recoveries exceed 50%, thus meeting the requirement for routine analysis. Introduction Solutions and standards A 1% formic acid solution in ACN was made fresh daily by The QuEChERS method was first introduced for the extraction adding 1 mL of formic acid to 100 mL of ACN, then mixing of pesticides from fruits and vegetables [1]. The QuEChERS well. A 1% acetic acid solution in ACN was made fresh daily methodology can be divided into two steps, extraction/parti- by adding 1 mL of acetic acid to 100 mL of ACN, then mixing tioning and dispersive SPE (d-SPE). In the first step, acetoni- well. -
Algorithmic Analysis of Chemical Dynamics of the Autoignition of NH3–H2O2/Air Mixtures
energies Article Algorithmic Analysis of Chemical Dynamics of the Autoignition of NH3–H2O2/Air Mixtures Ahmed T. Khalil 1,2, Dimitris M. Manias 3, Efstathios-Al. Tingas 4, Dimitrios C. Kyritsis 1,2,* and Dimitris A. Goussis 1,2 1 Department of Mechanical Engineering, Khalifa University of Science and Technology, Abu Dhabi 127788, UAE; [email protected] (A.T.K.); [email protected] (D.A.G.) 2 Research and Innovation Center on CO2 and H2 (RICH), Khalifa University of Science and Technology, P.O. Box 127788, Abu Dhabi, UAE 3 Department of Mechanics, School of Applied Mathematics and Physical Sciences, National Technical University of Athens, 157 73 Athens, Greece; [email protected] 4 Perth College, University of the Highlands and Islands, (UHI), Perth PH1 2NX, UK; [email protected] * Correspondence: [email protected] Received: 8 September 2019; Accepted: 7 October 2019; Published: 21 November 2019 Abstract: The dynamics of a homogeneous adiabatic autoignition of an ammonia/air mixture at constant volume was studied, using the algorithmic tools of Computational Singular Perturbation. Since ammonia combustion is characterized by both unrealistically long ignition delays and elevated NOx emissions, the time frame of action of the modes that are responsible for ignition was analyzed by calculating the developing time scales throughout the process and by studying their possible relation to NOx emissions. The reactions that support or oppose the explosive time scale were identified, along with the variables that are related the most to the dynamics that drive the system to an explosion. -
Kinetics of the Uncatalyzed, Alkaline Decomposition of Hydrogen Peroxide Trice Walter Haas Iowa State University
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1960 Kinetics of the uncatalyzed, alkaline decomposition of hydrogen peroxide Trice Walter Haas Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Physical Chemistry Commons Recommended Citation Haas, Trice Walter, "Kinetics of the uncatalyzed, alkaline decomposition of hydrogen peroxide " (1960). Retrospective Theses and Dissertations. 2645. https://lib.dr.iastate.edu/rtd/2645 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. KINETICS OF THE UN CATALYZED, ALKALINE DECOMPOSITION OF HYDROC-EN PEROXIDE by Trice Walter Haas A Dissertation Submitted to the Graduate Faculty in Partial Fulfillment of The Requirements for the Degree of DOCTOR OF PHILOSOPHY Major Subject: Physical Chemistry Approved: Signature was redacted for privacy. In Charge of Major Work Signature was redacted for privacy. Head of Major Department Signature was redacted for privacy. Iowa State University Of Science and Technology Ames, Iowa I960 il TABLE OP CONTENTS Page I. INTRODUCTION 1 II. EXPERIMENTAL 8 A. Apparatus 8 B. Quenching Technique 9 C. Analytical Techniques 10 D. Purification Methods 13 III. RESULTS AND DISCUSSION 20 A. The Homogeneous, Uncatalyzed Decomposition 20 1» General 20 2. Impurity effects 20 3* Surface effects 22 L Effect of light 27 5. Inert ions 28 6. Experimental results and discussion 29 7* Sources of error $1 B.