Title Reaction Between Ammonia and Carbon Dioxide Under High
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Phosphine and Ammonia Photochemistry in Jupiter's
40th Lunar and Planetary Science Conference (2009) 1201.pdf PHOSPHINE AND AMMONIA PHOTOCHEMISTRY IN JUPITER’S TROPOSPHERE. C. Visscher1, A. D. Sperier2, J. I. Moses1, and T.C. Keane3. 1Lunar and Planetary Institute, USRA, 3600 Bay Area Blvd., Houston, TX 77058-1113 2Baylor University, Waco, TX 76798, 3Department of Chemistry and Physics, The Sage Colleges, Troy, NY 12180, ([email protected], [email protected]) Introduction: The last comprehensive photo- tions involving the amino radical (NH2) play a larger chemical model for Jupiter’s troposphere was pre- role. We note that this is the first photochemical sented by Edgington et al. [1,2], based upon the work model to include P2H as an intermediate species in PH3 of Atreya et al. [3] and Kaye and Strobel [4-6]. Since photolysis. The equivalent N2Hx species are believed these early studies, numerous laboratory experiments to be important in the combustion chemistry of nitro- have led to an improvement in our understanding of gen compounds [15]. PH3, NH3-PH3, and NH3-C2H2 photochemistry [7-13]. Furthermore, recent Galileo, Cassini, and Earth-based observations have better defined the abundance of key atmospheric constituents as a function of altitude and latitude in Jupiter’s troposphere. These new results provide an opportunity to test and improve theoretical models of Jovian atmospheric chemistry. We have therefore developed a photochemical model for Jupi- ter’s troposphere considering the updated experimental and observational constraints. Using the Caltech/JPL KINETICS code [14] for our photochemical models, our basic approach is two- fold. The validity of our selected chemical reaction list is first tested by simulating the laboratory experiments of PH3, NH3-PH3, and NH3-C2H2 photolysis with pho- tochemical “box” models. -
Ammonia As a Refrigerant
1791 Tullie Circle, NE. Atlanta, Georgia 30329-2305, USA www.ashrae.org ASHRAE Position Document on Ammonia as a Refrigerant Approved by ASHRAE Board of Directors February 1, 2017 Expires February 1, 2020 ASHRAE S H A P I N G T O M O R R O W ’ S B U I L T E N V I R O N M E N T T O D A Y © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. COMMITTEE ROSTER The ASHRAE Position Document on “Ammonia as a Refrigerant” was developed by the Society’s Refrigeration Committee. Position Document Committee formed on January 8, 2016 with Dave Rule as its chair. Dave Rule, Chair Georgi Kazachki IIAR Dayton Phoenix Group Alexandria, VA, USA Dayton, OH, USA Ray Cole Richard Royal Axiom Engineers, Inc. Walmart Monterey, CA, USA Bentonville, Arkansas, USA Dan Dettmers Greg Scrivener IRC, University of Wisconsin Cold Dynamics Madison, WI, USA Meadow Lake, SK, Canada Derek Hamilton Azane Inc. San Francisco, CA, USA Other contributors: M. Kent Anderson Caleb Nelson Consultant Azane, Inc. Bethesda, MD, USA Missoula, MT, USA Cognizant Committees The chairperson of Refrigerant Committee also served as ex-officio members: Karim Amrane REF Committee AHRI Bethesda, MD, USA i © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. HISTORY of REVISION / REAFFIRMATION / WITHDRAWAL -
Safer Cocktail for an Ethanol/Water/Ammonia Solvent
L A S C P LSC in Practice C P O C L Safer Cocktail for an Ethanol/Water/ K T I A I C Ammonia Solvent Mixture L S A Problem T A laboratory had been under pressure to move towards Using this mixture, the sample uptake capacity of I the newer generation of safer liquid scintillation ULTIMA-Flo AP, ULTIMA-Flo M and ULTIMA Gold O cocktails. Unfortunately, the sample composition of LLT (PerkinElmer 6013599, 6013579 and 6013377, one of their targets kept giving the researchers problems. respectively) at 20 °C was determined and N Before the lead researcher contacted PerkinElmer, the results were: they had tried PerkinElmer’s Opti-Fluor®, ULTIMA ULTIMA-Flo AP 4.00 mL in 10 mL cocktail N Gold LLT, and ULTIMA Gold XR. All of the safer O ™ ULTIMA-Flo M 4.25 mL in 10 mL cocktail cocktails could incorporate each of the constituents T as indicated by their sample capacity graphs. ULTIMA Gold LLT 4.25 mL in 10 mL cocktail E The problematic sample was an extraction solvent From these results, we observed that it was possible consisting of 900 mL ethanol, 50 mL ammonium to get 4.0 mL of the sample into all of these cocktails. hydroxide, 500 mL water and an enzyme containing In addition, we determined that it was not possible to 14C. The mixture had a pH in the range of 10 to 11. get 4 mL sample into 7 mL of any of these cocktails. To complete this work, we also checked for lumines- Discussion cence using 4 mL of sample in 10 mL of each cocktail. -
Improving the Efficiency of Ammonia Electrolysis for Hydrogen Production
Improving The Efficiency Of Ammonia Electrolysis For Hydrogen Production A dissertation presented to the faculty of the Russ College of Engineering and Technology of Ohio University In partial fulfillment of the requirements for the degree Doctor of Philosophy Ramasamy Palaniappan December 2013 © 2013 Ramasamy Palaniappan. All Rights Reserved. 2 This dissertation titled Improving the Efficiency of Ammonia Electrolysis for Hydrogen Production by RAMASAMY PALANIAPPAN has been approved for the Department of Chemical and Biomolecular Engineering and the Russ College of Engineering and Technology by Gerardine G. Botte Professor of Chemical and Biomolecular Engineering Dennis Irwin Dean, Russ College of Engineering and Technology 3 ABSTRACT PALANIAPPAN, RAMASAMY, Ph.D., December 2013, Chemical Engineering Improving the Efficiency of Ammonia Electrolysis for Hydrogen Production Director of Dissertation: Gerardine G. Botte Given the abundance of ammonia in domestic and industrial wastes, ammonia electrolysis is a promising technology for remediation and distributed power generation in a clean and safe manner. Efficiency has been identified as one of the key issues that require improvement in order for the technology to enter the market phase. Therefore, this research was performed with the aim of improving the efficiency of hydrogen production by finding alternative materials for the cathode and electrolyte. 1. In the presence of ammonia the activity for hydrogen evolution reaction (HER) followed the trend Rh>Pt>Ru>Ni. The addition of ammonia resulted in lower rates for HER for Pt, Ru, and Ni, which have been attributed to competition from the ammonia adsorption reaction. 2. The addition of ammonia offers insight into the role of metal-hydrogen underpotential deposition (M-Hupd) on HER kinetics. -
Cellulosic Ethanol Production Via Aqueous Ammonia Soaking Pretreatment and Simultaneous Saccharification and Fermentation Asli Isci Iowa State University
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 2008 Cellulosic ethanol production via aqueous ammonia soaking pretreatment and simultaneous saccharification and fermentation Asli Isci Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Agriculture Commons, and the Bioresource and Agricultural Engineering Commons Recommended Citation Isci, Asli, "Cellulosic ethanol production via aqueous ammonia soaking pretreatment and simultaneous saccharification and fermentation" (2008). Retrospective Theses and Dissertations. 15695. https://lib.dr.iastate.edu/rtd/15695 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]. Cellulosic ethanol production via aqueous ammonia soaking pretreatment and simultaneous saccharification and fermentation by Asli Isci A dissertation submitted to the graduate faculty in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Co-majors: Agricultural and Biosystems Engineering; Biorenewable Resources and Technology Program of Study Committee: Robert P. Anex, Major Professor D. Raj Raman Anthony L. Pometto III. Kenneth J. Moore Robert C. Brown Iowa State University Ames, Iowa -
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. -
Ocean Storage
277 6 Ocean storage Coordinating Lead Authors Ken Caldeira (United States), Makoto Akai (Japan) Lead Authors Peter Brewer (United States), Baixin Chen (China), Peter Haugan (Norway), Toru Iwama (Japan), Paul Johnston (United Kingdom), Haroon Kheshgi (United States), Qingquan Li (China), Takashi Ohsumi (Japan), Hans Pörtner (Germany), Chris Sabine (United States), Yoshihisa Shirayama (Japan), Jolyon Thomson (United Kingdom) Contributing Authors Jim Barry (United States), Lara Hansen (United States) Review Editors Brad De Young (Canada), Fortunat Joos (Switzerland) 278 IPCC Special Report on Carbon dioxide Capture and Storage Contents EXECUTIVE SUMMARY 279 6.7 Environmental impacts, risks, and risk management 298 6.1 Introduction and background 279 6.7.1 Introduction to biological impacts and risk 298 6.1.1 Intentional storage of CO2 in the ocean 279 6.7.2 Physiological effects of CO2 301 6.1.2 Relevant background in physical and chemical 6.7.3 From physiological mechanisms to ecosystems 305 oceanography 281 6.7.4 Biological consequences for water column release scenarios 306 6.2 Approaches to release CO2 into the ocean 282 6.7.5 Biological consequences associated with CO2 6.2.1 Approaches to releasing CO2 that has been captured, lakes 307 compressed, and transported into the ocean 282 6.7.6 Contaminants in CO2 streams 307 6.2.2 CO2 storage by dissolution of carbonate minerals 290 6.7.7 Risk management 307 6.2.3 Other ocean storage approaches 291 6.7.8 Social aspects; public and stakeholder perception 307 6.3 Capacity and fractions retained -
BENZENE Disclaimer
United States Office of Air Quality EPA-454/R-98-011 Environmental Protection Planning And Standards June 1998 Agency Research Triangle Park, NC 27711 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF BENZENE Disclaimer This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and has been approved for publication. Mention of trade names and commercial products does not constitute endorsement or recommendation of use. EPA-454/R-98-011 ii TABLE OF CONTENTS Section Page LIST OF TABLES.....................................................x LIST OF FIGURES.................................................. xvi EXECUTIVE SUMMARY.............................................xx 1.0 PURPOSE OF DOCUMENT .......................................... 1-1 2.0 OVERVIEW OF DOCUMENT CONTENTS.............................. 2-1 3.0 BACKGROUND INFORMATION ...................................... 3-1 3.1 NATURE OF POLLUTANT..................................... 3-1 3.2 OVERVIEW OF PRODUCTION AND USE ......................... 3-4 3.3 OVERVIEW OF EMISSIONS.................................... 3-8 4.0 EMISSIONS FROM BENZENE PRODUCTION ........................... 4-1 4.1 CATALYTIC REFORMING/SEPARATION PROCESS................ 4-7 4.1.1 Process Description for Catalytic Reforming/Separation........... 4-7 4.1.2 Benzene Emissions from Catalytic Reforming/Separation .......... 4-9 4.2 TOLUENE DEALKYLATION AND TOLUENE DISPROPORTIONATION PROCESS ............................ 4-11 4.2.1 Toluene Dealkylation -
Titanium Dioxide Production Final Rule: Mandatory Reporting of Greenhouse Gases
Titanium Dioxide Production Final Rule: Mandatory Reporting of Greenhouse Gases Under the Mandatory Reporting of Greenhouse Gases (GHGs) rule, owners or operators of facilities that contain titanium dioxide production processes (as defined below) must report emissions from titanium dioxide production and all other source categories located at the facility for which methods are defined in the rule. Owners or operators are required to collect emission data; calculate GHG emissions; and follow the specified procedures for quality assurance, missing data, recordkeeping, and reporting. How Is This Source Category Defined? The titanium dioxide production source category consists of any facility that uses the chloride process to produce titanium dioxide. What GHGs Must Be Reported? Each titanium dioxide production facility must report carbon dioxide (CO2) process emissions from each chloride process line. In addition, each facility must report GHG emissions for other source categories for which calculation methods are provided in the rule. For example, facilities must report CO2, nitrous oxide (N2O), and methane (CH4) emissions from each stationary combustion unit on site by following the requirements of 40 CFR part 98, subpart C (General Stationary Fuel Combustion Sources). Please refer to the relevant information sheet for a summary of the rule requirements for calculating and reporting emissions from any other source categories at the facility. How Must GHG Emissions Be Calculated? Reporters must calculate CO2 process emissions using one of two methods, as appropriate: • Installing and operating a continuous emission monitoring system (CEMS) according to the requirements specified in 40 CFR part 98, subpart C. • Calculating the process CO2 emissions for each process line using monthly measurements of the mass and carbon content of calcined petroleum coke. -
Recent Advances in Tio2-Based Photocatalysts for Reduction of CO2 to Fuels
nanomaterials Review Recent Advances in TiO2-Based Photocatalysts for Reduction of CO2 to Fuels 1,2, 3, 4 5 Thang Phan Nguyen y, Dang Le Tri Nguyen y , Van-Huy Nguyen , Thu-Ha Le , Dai-Viet N. Vo 6 , Quang Thang Trinh 7 , Sa-Rang Bae 8, Sang Youn Chae 9,* , Soo Young Kim 8,* and Quyet Van Le 3,* 1 Laboratory of Advanced Materials Chemistry, Advanced Institute of Materials Science, Ton Duc Thang University, Ho Chi Minh City 700000, Vietnam; [email protected] 2 Faculty of Applied Sciences, Ton Duc Thang University, Ho Chi Minh City 700000, Vietnam 3 Institute of Research and Development, Duy Tan University, Da Nang 550000, Vietnam; [email protected] 4 Key Laboratory of Advanced Materials for Energy and Environmental Applications, Lac Hong University, Bien Hoa 810000, Vietnam; [email protected] 5 Faculty of Materials Technology, Ho Chi Minh City University of Technology (HCMUT), Vietnam National University–Ho Chi Minh City (VNU–HCM), 268 Ly Thuong Kiet, District 10, Ho Chi Minh City 700000, Vietnam; [email protected] 6 Center of Excellence for Green Energy and Environmental Nanomaterials (CE@GrEEN), Nguyen Tat Thanh University, 300A Nguyen Tat Thanh, District 4, Ho Chi Minh City 755414, Vietnam; [email protected] 7 Cambridge Centre for Advanced Research and Education in Singapore (CARES), Campus for Research Excellence and Technological Enterprise (CREATE), 1 Create Way, Singapore 138602, Singapore; [email protected] 8 Department of Materials Science and Engineering, Korea University, 145 Anam-ro, Seongbuk-gu, Seoul 02841, Korea; [email protected] 9 Department of Materials Science, Institute for Surface Science and Corrosion, University of Erlangen-Nuremberg, Martensstrasse 7, 91058 Erlangen, Germany * Correspondence: [email protected] (S.Y.C.); [email protected] (S.Y.K.); [email protected] (Q.V.L.); Tel.: +42-01520-2145321 (S.Y.C.); +82-109-3650-910 (S.Y.K.); +84-344-176-848 (Q.V.L.) These authors contributed equally to this work. -
Carbon Dioxide Exposure Effects – Fact Sheet
CARBON DIOXIDE EXPOSURE EFFECTS – FACT SHEET Studies by NIOSH in 1976 dispelled the myth that carbon dioxide is an asphyxiant gas and only causes adverse health effects when it displaces oxygen. Symptoms of overexposure by inhalation include dizziness, headache, nausea, rapid breathing, shortness of breath, deeper breathing, increased heart rate (tachycardia), eye and extremity twitching, cardiac arrhythmia, memory disturbances, lack of concentration, visual and hearing disturbances (including photophobia, blurred vision, transient blindness, hearing loss and ringing in the ears), sweating, restlessness, vomiting, shaking, confusion, flushed skin, panic, parathesis (a sensation of numbness in the extremities), disorientation, convulsions, unconsciousness, coma, and death. CO2 Duration Physiological Impact/Health Effect Concentration 1,000 ppm Less than Impairs judgment, decision-making ability, and thinking skills on a 2½ hrs. short-term basis, even for healthy individuals. 2,500 ppm Less than Many individuals are rendered cognitively marginal or 2½ hrs. dysfunctional. 5,000 ppm with Headache, lethargy, mental slowness, emotional irritation, and 20.9% Oxygen sleep disruption. 6% 1-2 mins. Hearing and visual disturbances 7% (70,000 ppm) 5 mins. death with 20.9% Oxygen 10% to 15% Dizziness, drowsiness, severe muscle twitching, unconsciousness and death within a few minutes. Within 1 Loss of controlled and purposeful activity, unconsciousness, coma, 17% to 30% min. convulsions, and death 30% carbon 30 secs. Unconsciousness, with some subjects having seizures that were dioxide, with 70% characterized as decerebrate (no cerebral functioning). oxygen Even though oxygen is necessary to carry out cell functions, it is not the lack of oxygen that stimulates breathing. Breathing is stimulated by an excess of CO2. -
What Are the Health Effects from Exposure to Carbon Monoxide?
CO Lesson 2 CARBON MONOXIDE: LESSON TWO What are the Health Effects from Exposure to Carbon Monoxide? LESSON SUMMARY Carbon monoxide (CO) is an odorless, tasteless, colorless and nonirritating Grade Level: 9 – 12 gas that is impossible to detect by an exposed person. CO is produced by the Subject(s) Addressed: incomplete combustion of carbon-based fuels, including gas, wood, oil and Science, Biology coal. Exposure to CO is the leading cause of fatal poisonings in the United Class Time: 1 Period States and many other countries. When inhaled, CO is readily absorbed from the lungs into the bloodstream, where it binds tightly to hemoglobin in the Inquiry Category: Guided place of oxygen. CORE UNDERSTANDING/OBJECTIVES By the end of this lesson, students will have a basic understanding of the physiological mechanisms underlying CO toxicity. For specific learning and standards addressed, please see pages 30 and 31. MATERIALS INCORPORATION OF TECHNOLOGY Computer and/or projector with video capabilities INDIAN EDUCATION FOR ALL Fires utilizing carbon-based fuels, such as wood, produce carbon monoxide as a dangerous byproduct when the combustion is incomplete. Fire was important for the survival of early Native American tribes. The traditional teepees were well designed with sophisticated airflow patterns, enabling fires to be contained within the shelter while minimizing carbon monoxide exposure. However, fire was used for purposes other than just heat and cooking. According to the historian Henry Lewis, Native Americans used fire to aid in hunting, crop management, insect collection, warfare and many other activities. Today, fire is used to heat rocks used in sweat lodges.