CM 4310, Green Engineering Fall 07 Homework #2 Mon. 03 Dec., ' Atom and Mass Efficiencies Problem 1 of Chapter 7, page 198.

Similar documents
Q1. The table shows how much carbon dioxide is produced when you transfer the same amount of energy by burning coal, gas and oil.

Greenhouse gases affect the temperature of the Earth. Which gas is a greenhouse gas? Tick one box. Argon Methane Nitrogen Oxygen

Onboard Plasmatron Generation of Hydrogen Rich Gas for Diesel Engine Exhaust Aftertreatment and Other Applications.

STATEMENT OF BASIS. Cherokee Nitrogen LLC Cherokee, Alabama Colbert County Facility Number

Replacement Tubes for Gillian Gas Detection Pumps

Module 6: Chemical Resistance

Biofine Technology, LLC

Q1. Useful fuels can be produced from crude oil. Crude oil is a mixture of hydrocarbons.

Sustainable Purchasing Guide Fuels

HYDROFLUORIC ACID FLUOROCARBONS AND PROCESS ECONOMICS PROGRAM. Report No. 89. November A private report by the MENLO PARK, CALIFORNIA

HYDROGEN PRODUCTION BY AQUEOUS-PHASE REFORMING OF GLYCEROL FROM THE BIODIESEL MANUFACTURING

Issue One. Chemical Compatibility Guide

2014 FCA Canada Inc. Windsor Assembly Plant [ANNUAL PUBLIC REPORT UNDER O. REG. 455/09]

Stephen Stanley Jose de Barros Fred Gardner Lummus Technology 1 st Indian Oil Petrochemical Conclave March 16, 2012 New Delhi

The table below gives information about milk bottles. Raw materials Sand, limestone, salt Crude oil. Bottle material Soda-lime glass HD poly(ethene)

Fuels are materials that are used to create energy. They may be

ETHYLENE-PROPYLENE PROCESS ECONOMICS PROGRAM. Report No. 29A. Supplement A. by SHIGEYOSHI TAKAOKA With contributions by KIICHIRO OHYA.

Fraction Distillation of Crude Oil

Biodiesel and SmartWay Grow and Go Go. EPA-MMTA Fuel-Saving Seminar June 15, 2007

Beverage Grade Carbon Dioxide

Edexcel GCSE Chemistry. Topic 8: Fuels and Earth science. Fuels. Notes.

Petroleum Refining Fourth Year Dr.Aysar T. Jarullah

Where We Are. Today: Finish up Chapter 4, hopefully! Discussion: Alternative fuels, the benefits of conservation Where to go next?

Selection of DODGE E-Z KLEEN Polymer and Stainless Steel Housed Ball Bearings. P = (X x F R ) + (Y x F A ) F A C o

PRICE LIST 2017/2018

Ducting & Ventilation Components

Envirochem Testing Lab & Research Centre, Plot No. 165, Sector-25, Part-II, HUDA, Panipat, Haryana. Discipline Chemical Testing Issue Date

M1.(a) C 6 H [5] Page 2. PhysicsAndMathsTutor.com

CH 6. S.S.E.R. Ltd. Registered in England & Wales. Company Registration No

Pressure switch FF 4 Approval acc. to ATEX EN For mining and chemistry

EXPERIMENTAL INVESTIGATION OF THE EFFECT OF HYDROGEN BLENDING ON THE CONCENTRATION OF POLLUTANTS EMITTED FROM A FOUR STROKE DIESEL ENGINE

Q1.This question is about the temperature of the Earth s atmosphere. Give one reason why it is difficult to produce models for future climate change.

Japan s s Experience in Alternative Transport Fuels: Successes and R&D Challenges

Total chemical production

About this document. This document contains screenshots of software available from Cheresources.com. You can find this title in our online store at:

CONTENTS. Chapter 1 Industrial Catalysts. Chapter 2 The First Catalysts

V.Venkatakranthi Teja. N S Raju Institute of Technology (NSRIT), Sontyam, Visakhapatnam, Andhra Pradesh , India.

Report No. 35 BUTADIENE. March A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I PARK, CALIFORNIA

Background on Biodiesel

HD and HDL Single-Stage Non-Lube Gas Compressors

MERCER VALVE GENERAL INFORMATION

SENSORS AND SYSTEMS FOR HUMIDITY AND TEMPERATURE MEASUREMENTS RELIABILITY REPORT. HS1100 / HS1101 Relative Humidity Capacitive Sensors

Supplement of Emission factors of black carbon and co-pollutants from diesel vehicles in Mexico City

Life-Cycle Energy and Greenhouse Gas Results of Fischer-Tropsch Diesel Produced from Natural Gas, Coal, and Biomass

New Catalytic Process Production of Olefins

3. Operation of any applicable boiler on any amount of fuel oil shall be prohibited, except as provided in Subsection C.3.

New Leaf Biofuel, LLC

Challenges and Solutions for Shale Oil Upgrading

C1.4 CRUDE OIL AND FUELS / C1.5 PRODUCTS FROM OIL

Preface... xii. 1. Refinery Distillation... 1

(Syn)Gas to Fuel HIGH QUALITY GASOLINE FROM METHANOL

Synonym(s) ) Chlorine, liquefied/gas. Ammonia, Gasoline, natural 7300 (gasoline) Hydrogen gas. Phosgene

Fundamentals of Petrochemical Industry

Battery. Student booklet

EMISSIONS CHARACTERIZATION OF AN AMMONIA-GASOLINE SI ENGINE

PRACTICE EXAMINATION QUESTIONS FOR 1.6 ALKANES (includes some questions from 1.5 Introduction to Organic Chemistry)

Studies on Emission Control in S.I. Engine Using Organic Fuel Additives

Brushwood-chulha Average (SD) Mixed-chulha Average (SD) Dung-angithi Average (SD) SOAP koh (x ) (cm 3 molec -1 s -1 )

CHAPTER 1 INTRODUCTION

SAMPLING CONTAINERS & HOLDING TIMES. Parameters Method Holding Time 8 Minimum Volume Water Sampling Water Soil Water Soil Container Preservative 9

Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES

gc applications Hydrocarbons C1-C5 Paraffins Hydrocarbons, Sulfur Gases C1-C2 Hydrocarbons Gases

Performance of a Compression-Ignition Engine Using Direct-Injection of Liquid Ammonia/DME Mixture

Zeolite Catalyst. Methanol. Propylene. Petrochemical Research & Technology پژوهش و فناوري پتروشیمی

Ontario Toxics Reduction Act Report (Ontario Regulation 455/09) - Nanticoke Refinery

Beyond Cold Gas Thrusters

Renewable Diesel & Biodiesel

Colorimetric Gas Detector Tube System US Dollar Price List

Models 910, 911, 916, 917, 920, 921, 927 ASME Section VIII, Air/Gas/

Biodiesel and Renewable Fuels

Direct Liquefaction of Biocoals as a Sustainable Route to Second-Generation Biofuels

Distillation process of Crude oil

Dräger CMS Chip Measurement System

Dräger CMS. Dräger CMS: Highly accurate and easy to use. Dräger CMS Chip: Miniaturised Dräger-Tubes.

Electronic Supplementary information

Recyclable Heterogeneous Copper Oxide on Alumina Catalyzed Coupling of Phenols and Alcohols with Aryl halides under Ligand Free Conditions

Abstract Process Economics Program Report No. 203 ALKANE DEHYDROGENATION AND AROMATIZATION (September 1992)

Oxidation Technologies for Stationary Rich and Lean Burn Engines

Annex to the Accreditation Certificate D-PL according to DIN EN ISO/IEC 17025:2005

Metallic Systems TYPE SPTC

Emission controls for NOx compliance Challenges & Applications. Greener Shipping Summit November 2017

X-STREAM Enhanced XEGP - General Purpose Gas Analyzer

CONVERSION OF GLYCEROL TO GREEN METHANOL IN SUPERCRITICAL WATER

State of the Art (SOTA) Manual for Internal Combustion Engines

SCOPE OF ACCREDITATION TO ISO/IEC 17025:2005

EXPLOSION-PROOF MOTORS SINGLE PHASE

Alcohols to Hydrocarbons (ATH)

Schedule of Accreditation issued by United Kingdom Accreditation Service 2 Pine Trees, Chertsey Lane, Staines-upon-Thames, TW18 3HR, UK

Module8:Engine Fuels and Their Effects on Emissions Lecture 36:Hydrocarbon Fuels and Quality Requirements FUELS AND EFFECTS ON ENGINE EMISSIONS

Gaseous fuel, production of H 2. Diesel fuel, furnace fuel, cracking

ZERO PILOT UNITS PIONEERING TECHNOLOGIES ON A SMALL SCALE.

Ecosteps Laboratory Pvt. Ltd., D-79, Sector-6, Noida, Uttar Pradesh. Discipline Chemical Testing Issue Date

DARS FUEL MODEL DEVELOPMENT

3.2 The alkanes. Isomerism: Alkanes with 4 or more carbons show a type of structural isomerism called chain isomerism

Fuels of the Future for Cars and Trucks

Optimization of Synthetic Oxygenated Fuels for Diesel Engines

GTC Technology Day. 16 April Hotel Le Meridien New Delhi. Isomalk Technologies for Light Naphtha Isomerization

ENGINEERING CALCULATION SHEET AIR RESOURCES DIVISION

Discipline Chemical Testing Issue Date Certificate Number T-3037 Valid Until Last Amended on - Page 1 of 6

Stoichiometry and Pollution Control

Transcription:

CM 4310, Green Engineering Fall 07 Homework #2 Mon. 03 Dec., '07 1. Atom and Mass Efficiencies Problem 1 of Chapter 7, page 198. 2. Criteria Pollutant Emissions from an Industrial Boiler (Chapter 8) Calculate criteria pollutant emissions (SO 2, NO x, CO, Filterable Particulate Matter) and CO 2 from an industrial facility using the following information. Low S No. 6 Oil (1% wt. Sulfur) Annual Energy Demand of 10 11 Btu/yr Heating Value of 150,000,000 Btu/10 3 gal Boiler Efficiency of 0.90 3. Life Cycle Assessment: Disposable versus Home Laundered Cloth Diapers Problem 2 from Chapter 13 of the text. Parts a) and b) only. Due Mon 10 Dec., '07

1. Atom and Mass Efficiency Calculations: Calculate mass and atom efficiencies a) (Addition reaction) Isobutylene + methanol methyl,tert-butyl ether C 4 H 8 + CH 3 OH (C 4 H 9 )-O-CH 3 Mass efficiency: Feedstocks 5(12) + 12(1) + 1(16) = 88 Product 5(12) + 12(1) + 1(16) = 88.. efficiency = 100% Carbon efficiency: Feedstocks 5(12) = 60 Product 5(12) = 60.. efficiency = 100% Hydrogen efficiency: Feedstocks 12(1) = 12 Product 12(1) = 12.. efficiency = 100% Oxygen efficiency: Feedstocks 1(16) = 16 Product 1(16) = 16.. efficiency = 100% b) (Substitution reaction) Phenol + ammonia aniline + water C 6 H 5 -OH + NH 3 C 6 H 5 -NH 2 + H 2 O Mass efficiency: Feedstocks 6(12) + 9(1) + 1(16) + 1(14) = 111 Product 6(12) + 7(1) + 0(16) + 1(14) = 93.. efficiency = 83.8% Carbon efficiency: Feedstocks 6(12) = 72 Product 6(12) = 72.. efficiency = 100% Hydrogen efficiency: Feedstocks 9(1) = 9 Product 7(1) = 7.. efficiency = 77.8% Oxygen efficiency: Feedstocks 1(16) = 16 Product 0(16) = 0.. efficiency = 0% Nitrogen efficiency: Feedstocks 1(14) = 14 Product 1(14) = 14.. efficiency = 100% c) (Elimination reaction) Ethylbenzene styrene + hydrogen C 6 H 5 -C 2 H 5 C 6 H 5 -C 2 H 3 + H 2 Mass efficiency: Feedstocks 8(12) + 10(1) = 106 Product 8(12) + 8(1) = 104.. efficiency = 98.1% Carbon efficiency: Feedstocks 8(12) = 96 Product 8(12) = 96.. efficiency = 100% Hydrogen efficiency: Feedstocks 10(1) = 10 Product 8(1) = 8.. efficiency = 80% d) Other industrially important examples of additions, substitutions, and elimination reactions (see Wittkcoff, H.A. and Reuben, B.G. Industrial Organic Chemicals, John Wiley & Sons, New York, 1996; and Weissermel, K. and Arpe, H.-J. Industrial Organic Chemistry, VCH Verlagsgesellschaft mbh a Wiley company, Weinheim Germany, 1997). Addition Reactions: Ethanol from ethene CH 2 =CH 2 + H 2 O C 2 H 5 OH (hydration of ethylene using a phosphoric acid catalyst, low per pass conversions on the order of 10%)

Mass efficiency: Feedstocks 2(12) + 6(1) + 1(16) = 46 Product 2(12) + 6(1) + 1(16) = 46.. efficiency = 100% Carbon efficiency: Feedstocks 2(12) = 24 Product 2(12) = 24.. efficiency = 100% Hydrogen efficiency: Feedstocks 6(1) = 6 Product 6(1) = 6.. efficiency = 100% Oxygen efficiency: Feedstocks 1(16) = 16 Product 1(16) = 16.. efficiency = 100% Ethylene oxide from ethene CH 2 =CH 2 + 0.5O 2 CH 2 CH 2 (silver catalyst, 15 bar and 250 C, yield > 80%) \ / O Mass efficiency: Feedstocks 2(12) + 4(1) + 1(16) = 44 Product 2(12) + 4(1) + 1(16) = 44.. efficiency = 100% Carbon efficiency: Feedstocks 2(12) = 24 Product 2(12) = 24.. efficiency = 100% Hydrogen efficiency: Feedstocks 4(1) = 4 Product 4(1) = 4.. efficiency = 100% Oxygen efficiency: Feedstocks 1(16) = 16 Product 1(16) = 16.. efficiency = 100% Vinyl chloride from acetylene CH CH + HCl CH 2 =CHCl Mass efficiency: Feedstocks 2(12) + 3(1) + 1(35.45) = 62.45 Product 2(12) + 3(1) + 1(35.45) = 62.45.. efficiency = 100% Carbon efficiency: Feedstocks 2(12) = 24 Product 2(12) = 24.. efficiency = 100% Hydrogen efficiency: Feedstocks 5(1) = 5 Product 5(1) = 5.. efficiency = 100% Chlorine efficiency: Feedstocks 1(35.45) = 35.45 Product 1(35.45) = 35.45.. efficiency = 100% Substitution Reactions: Vinyl chloride from ethene CH 2 =CH 2 + Cl 2 CH 2 ClCH 2 Cl CH 2 =CHCl + HCl Mass efficiency: Feedstocks 2(12) + 4(1) + 2(35.45) = 98.45 Product 2(12) + 3(1) + 1(35.45) = 62.45.. efficiency = 63.4% Carbon efficiency: Feedstocks 2(12) = 24 Product 2(12) = 24.. efficiency = 100% Hydrogen efficiency: Feedstocks 4(1) = 4 Product 3(1) = 3.. efficiency = 75% Chlorine efficiency: Feedstocks 2(35.45) = 70.9 Product 1(35.45) = 35.45.. efficiency = 50%

Chlorine from oxidation of HCl 4HCl + O 2 2H 2 O + 2Cl 2 Mass efficiency: Feedstocks 4(1) + 4(35.45) + 1(32) = 217.8 Product 2(70.9) = 141.8.. efficiency = 65.1% Hydrogen efficiency: Feedstocks 4(1) = 4 Product 0(1) = 0.. efficiency = 0% Chlorine efficiency: Feedstocks 4(35.45) = 141.8 Product 2(70.9) = 141.8.. efficiency = 100% Oxygen efficiency: Feedstocks 1(32) = 32 Product 0(32) = 0.. efficiency = 0% Vinyl chloride from ethylene using oxychlorination (By integrating the above two reactions, we can increase the mass efficiency of the overall production of vinyl chloride) 1.5CH 2 =CH 2 + 1.5Cl 2 1.5CH 2 ClCH 2 Cl 3CH 2 ClCH 2 Cl 3CH 2 =CHCl + 3 HCl 1.5CH 2 =CH 2 + 3HCl + 0.75O 2 1.5CH 2 ClCH 2 Cl + 1.5H 2 O Mass efficiency: Feedstocks 6(12) + 15(1) + 6(35.45) + 1.5(16) = 333.7 Product 6(12) + 15(1) + 6(35.45) + 0(16) = 309.7.. efficiency = 92.8% Carbon efficiency: Feedstocks 6(12) = 72 Product 6(12) = 72.. efficiency = 100% Hydrogen efficiency: Feedstocks 15(1) = 15 Product 15(1) = 15.. efficiency = 100% Chlorine efficiency: Feedstocks 6(35.45) = 222.7 Product 6(35.45) = 222.7.. efficiency = 100% Oxygen efficiency: Feedstocks 1.5(16) = 24 Product 0(16) = 0.. efficiency = 0% Elimination Reactions: Phenol from dehydrogenation of a cyclohexanone/cyclohexanol mixture =O + 2 OH OH + 9/2 H Mass efficiency: Feedstocks 12(12) + 11(1) + 2(16) = 187 Product 12(12) + 2(1) + 2(16) = 178.. efficiency = 95.2% Carbon efficiency: Feedstocks 12(12) = 144 Product 12(12) = 144.. efficiency = 100%

Hydrogen efficiency: Feedstocks 11(1) = 11 Product 2(1) = 2.. efficiency = 18.2% Oxygen efficiency: Feedstocks 2(16) = 32 Product 2(16) = 32.. efficiency = 100%

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

3. Life-Cycle Assessment of Diapering Systems a) Diapers per baby per week for disposable diapers Equivalency of diapers 15.8 billion disposable diapers are sold annually 3,787,000 babies are born each year children wear diapers for the first 30 months disposable diapers are used on 85% of children. Number of babies in diapers = (3,787,000 babies born/yr)(30 mo. in diapers/12 mo/yr) = 9,467,500 Number of babies in disposable diapers = 9,467,500 babies(0.85) = 8,047,375 Number of disposable diapers per baby per year = (15.8x10 9 disposable diapers)/(8,047,375 babies) = 1,963.4 disposable diapers/baby Number of disposable diapers per baby per week = (1,963.4 disposable diapers/baby)/52 weeks = 39.3 Equivalence = (39.3 disposable diapers/baby/wk)/(68 cloth diapers/baby/wk) = 0.577 b) Complete the Table of Ratio of Impact to Home Laundered Impact Impact Disposable diapers Commercially laundered cloth Home laundered Cloth diapers diapers Energy requirements (million BTU) 0.52 0.55 1.0 Solid waste (cubic feet) 4.26 1.0 1.0 Atmospheric emissions (lb) 0.50 0.47 1.0 Waterborne wastes (lb) 0.14 0.95 1.0 Water requirements (gal) 0.28 1.26 1.0 c) Recycle Percentage for Disposable Diapers 20 Solid Waste per 1000 Diapers 16 12 y = -0.162x + 17.04 R 2 = 1 8 4 0 0 20 40 60 80 100 120 % Recycle

The recycle percentage needed for disposable diapers to equal the solid waste requirements of laundered cloth diapers (2.3 cubic feet) can be obtained from the best-fit equation in the figure above. Rearranging the trendline from able and solving for x, x = (17.04-2.3)/0.163 = 90.43%.