operate regenerator top without boiling aq. amine solution.
|
|
- Jeffrey Warner
- 6 years ago
- Views:
Transcription
1 HSRemoval-MaterialBalacemcd Rough material balace for removal of H S from shale gas with MDEA ad recovery of elemetal sulfur via the Claus process The solvet has bee dow-selected to be methyldiethaolamie (MDEA) Step remove H S with a absorber Step regeerate solvet by releasig captured H S with distillatio Step covert captured H S to elemetal sulfur S Specificatios rocess iput: Shale gas ~ millio stadard cubic feet/day (MMscfd) shale gas 7 ppm (by volume) H S ad % (by volume) CO Assume shale gas remaiig compositio is 9% (by volume) CH 4, % C H 6 Gas is available at 7 F, 96 psia rocess output: pipelie quality atural gas <4 ppmv H S ad <% (by volume) CO <7 lbs water/ millio scf Gas should be delivered at 6 psia, 7 F recover elemetal sulfur S Istructor: Nam Su Wag Thermophysical data MDEA (-methyldiethaolamie) = CH N-(CH CH OH) = C H NO MW MDEA 96 MW HO 8 boilig poit & freezig poit bp MDEA 47 C mp MDEA C boilig poit & freezig poit bp HO C mp HO C operate absorber i this rage Assume o chage i volume upo mixig specific gravity ρ water g/cm ρ MDEA 4 g/cm operate regeerator top without boilig aq amie solutio The followig specificatio ot used (util gas is throttled to 6psia) Alteratively, throttle sour gas to 6psia ad operate the absorber at 6psia Higher pressure helps gas absorptio, but icreases equipmet cost totalout 6 psia rocess flow diagram Chemical compoets compoet stream 8 ( total CH4 CH6 CO HO HS MDEA SO S O N ) ( i ) compoet ( dummy amier amiel furace claus ) ( ) j stream iitialize storage space for mole umber ad pressure compoet, stream compoet, stream
2 HSRemoval-MaterialBalacemcd Natural gas basis: mole basis 7 ppm (by volume) H S ad % (by volume) CO remaiig compositio is 9% (by volume) CH 4, % C H 6 Assume ideal gas i traslatig volume % to mole % ad partial pressure HS, CH6, total, total, basis = basis 7 6 = 7 basis basis i, total, HS, HS, 9 = 8768 HS, CH6, = 974 = 96 psia i, total, total, total, 4696 total, = a Absorber -- top at T=~4~ C Assume very little pressure drop i the absorber, compared to the absolute pressure total, Assume hydrocarbos CH 4 & C H 6 do ot dissolve i aq MDEA solvet, ad most of this shale gas stream is CH 4 & C H 6 CH6, CH6, Assume CO =% vol CH6, The rest are i very small amouts CH6, = 8768 = 974 = a 98 CH6, Saturated with H O wrt % H i liquid at 4 C; HO =689psia This is H O lost to the product stream ad is to be made-up total, total, = 768 a = = 988
3 HSRemoval-MaterialBalacemcd We ca assume the product gas cotais H S saturated wrt wt% aq MDEA solutio; or we ca assume the specificatio level: H S=4ppmv I the fial desig, we wat to stay ot exactly at this specificatio level but a bit below this specificatio level to allow for process fluctuatios HS, HS, 4 6 HS, HS, = 6469 a HS, Assume at 4 C, vapor pressure of MDEA is mmhg This is MDEA lost to the product stream ad is to be made-up total, 76 total, = = 6664 a = = 994 total, Absorber -- top; amie-lea stream Assume aq amie solutio recirculatio = mole aq amie solutio per mole of gas Sice there is ot as much CO i this problem compared to flue gas or sygas, the amie solutio circulatio could be a bit less i the fial desig MDEA HO basis Assume wt% aqueous amie solvet; wt MDEA :wt HO =: (based o weight) MDEA MW MDEA fractio MDEA MW wt fractio wt MDEA HO MW HO Give the above two equatios, we have: fractio wt MW HO basis = amiel MW MDEA fractio wt MW amiel MDEA fractio wt MW HO amiel fractio wt MW MDEA basis = MW MDEA fractio wt MW amiel MDEA fractio wt MW HO We assume ~% of H S & ~% of CO is stripped off i the solvet regeerator; a small amout of H S ad a small amout of CO may remai i the lea aqueous amie solutio Of course, we ca assume ay other degree of strippig as well, say, 9% removal of acid gas i the regeerator Alterately, we ca substitute this assumptio with oe that assumes the amie solutio is saturated wrt H S i the vapor phase (which meas a loadig of ~mole H S/mole amie i the rich-amie stream) HS, amiel amiel total, amiel amiel = total, amiel
4 4 HSRemoval-MaterialBalacemcd Absorber -- bottom; amie-rich stream at T=~4~ C (more acid gas absorbed but slower rate at low T) material balace o the absorber i, amier i, i, amiel, i = HS, amier 7 = amier Solubility of H S ad CO i aq MDEA solutio At wt% aq MDEA solutio, HS =ka of H S correspods to loadig of ~ mole H S/mole amie ( C~4 C), with higher loadig at lower T (data from Li & She, J Chem Eg Data, 8, -8, 99, Fig ) We ca apply a loadig of mole H S/mole amie at HS =ka (data from Huttehuis et al, J etroleum Sci Egi,, -4, 7, Fig ) Here, we merely check to see if we are withi the saturated loadig limits If the umbers are ureasoable, we adjust the amout of recirculatig amie absorber HS, = 496 a HS, amier saturatio loadig (mole HS/mole amie)=~: = 6 amier check Let us apply a theoretical loadig of mole CO/mole amie at CO =7ka (data from Huttehuis et al, J etroleum Sci Egi,, -4, 7, Fig ) = 64 loadig (mole CO/mole amie): amier amier amier amier amier However, this far exceeds the amout of CO i the ; thus, selective removal of oly H S is questioable at equilibrium with the amout of amie we circulate It is possible if selective removal is kietically govered; that is, kietics of absorptio of CO is sufficietly slow compared to that of H S We ca reduce the amout of amie if we allow a very log time for equilibrium (thus, a very large absorber), or we recirculate a excess amout of amie to offset a fractioal approach toward equilibrium for CO = For ow, we ca assume either all CO i the gas dissolves i amie, or oly the balace amout (after subtractig CO i the product gas) dissolves i amie amier amiel With the latter assumptio, the CO loadig is: amier amier total, amier amier = = 9 oly a fractio of the theoretical loadig of CO :MDEA=: amier = 87 total, amier = bad
5 HSRemoval-MaterialBalacemcd Regeerator -- distillatio at T bottom =~ C, T top =below C (high T to drive off acid gas without boilig the aqueous amie solvet, which is mostly water based o mole fractio ad defiitely above freezig of water at C); pick T=~ C as a first approximatio The off gas from the codeser is saturated with water vapor ad MDEA vapor (which is egliget) Assume bottom =~atm, top =~atm; T top goes ito estimatig the relatively small amout of water vapor ad MDEA vapor; ad top gives a rough estimate of relative error whe igorig water vapor (which is roughly ~% error) material balace o the regeerator i, i, amier i, amiel total, If we igore HO vapor, = Saturated with H O wrt % H i liquid at C; HO =788psia This is H O lost to the off gas stream ad is to be made-up HS, HS, total, = 4 a total, a = We ca go back to the lea amie stream ad correct for the above small amout of water ( mole out of ~87 mole), but that is ot at all sigificat Assume at C, vapor pressure of MDEA is mmhg This is MDEA lost to the off gas stream ad is to be made-up 76 total, = 6664 a = material balace o the regeerator (with a bit of water i off gas stream) total,
6 6 HSRemoval-MaterialBalacemcd Claus reactor Claus Reactio : H S + O SO + H O + heat Claus Reactio H S + SO S + H O + heat Overall (Step + X Step): 6 H S + O 6 S + 6 H O Re-write the above reactios Claus Reactio : / H S + / O / SO + / H O + heat Claus Reactio / H S + / SO S + / H O + heat Overall (Step + Step): H S + / O S + H O ossible udesirable side reactio : SO + / O SO (fid a coditio to miimize this later) Reactio stoichiometry Reactio Reactio HS, HS, O, SO, SO,, S total, total, 6 compoet, Assume we provide stoichiometric amout of oxyge (i the form of ) eeded to react with H S The amout of HS to be reacted is based o equilibrium at the lastlaus step, which i practice is equivalet to ~9% coversio of H S to elemetal S I other type of reactios, we ormally provide extra oxyge (perhaps % excess) to push for complete combustio of the fuel However, i this problem, we wat to avoid geeratig excess SO with excess O, because SO is ot the desired fial product I the fial desig, we should iclude a cotroller for ig O to the furace based o H S measuremet O, HS, N, total, 79 O, O, N, = 7 = 4 = 79 total, Assume complete combustio i the furace at T=flame temperature ε O, = O, material balace for the furace ε 7 extet of Claus Reactio to completely cosume O furace < > < > ε We the cool dow the furace exhaust to as low T as possible to favor equilibrium coversio but ~ C above the dew poit of S i subsequet reactors (dew poit at ~ C) to avoid codesig S o catalyst ad deactivatig catalyst 9 ε HS, ε = S, claus < furace > ε 7 extet of Claus Reactio to covert 9% of H S to elemetal S
7 7 HSRemoval-MaterialBalacemcd Summary of molar flow rates: colums=streams = (iput) = =amier 4=amieL = (output) 6= 7=furace 8=claus (output) rows=compoets =total =CH4 =CH6 =CO 4=HO =HS 6=MDEA 7=SO 8=S 9=O =N ( dummy amier amiel furace claus ) = total CH4 CH6 CO HO HS MDEA SO S O N
1. Write down the ideal gas law and define all its variable and parameters. 2. Calculate the values and units of the ideal gas law constant R.
Ideal Gases Objectives:. Write dow the ideal gas law ad defie all its variable ad parameters.. Calculate the values ad uits of the ideal gas law costat R. 3. Calculate the value of oe variable,, T, or,
More informationSeated valves (PN 16) VF 2-2-way valve, flange VF 3-3-way valve, flange
Data sheet Seated valves (PN 16) VF 2-2-way valve, flage VF 3-3-way valve, flage Descriptio Features: Bubble tight desig 15-80, 200-300 Sap mechaical coectio together with AMV(E) 335, AMV(E) 435 Dedicated
More informationPREPARING SOLUBILITY DATA FOR USE UPDATING KEY RESOURCES BY THE GAS PROCESSING INDUSTRY:
PREPARING SOLUBILITY DATA FOR USE Mapping Midstream s Future 2012 GPA Convention BY THE GAS PROCESSING INDUSTRY: UPDATING KEY RESOURCES Darryl Mamrosh and Kevin Fisher Trimeric Corporation Jeff Matthews
More informationA Comparative Investigation of Reheat In Gas Turbine Cycles
Proceedigs of the Iteratioal Gas Turbie ogress 3 Tokyo November -7, 3 IGT3Tokyo TS-86 A omparative Ivestigatio of Reheat I Gas Turbie ycles K. Sarabchi Departmet of Mechaical egieerig Uiversity of Tabriz
More informationn UL Listed and FM Approved for n Solenoid control n Quick pressure relief valve 73Q n Pressure sustaining & reducing valve 723
Pressure Relief/Sustaiig Valve Prioritizig pressure zoes Esurig cotrolled pipelie fill-up Prevetig pipelie emptyig Pump overload & cavitatio protectio Safeguardig pump miimum flow Excessive lie pressure
More informationFootwork is the foundation for a skilled basketball player, involving moves
The Complete Book of Offesive Basketball Drills Basic Footwork ad Cuts Drills 2 Equipmet 16 chairs (or less) Persoel The etire team Basic Footwork ad Cuts Drills Two coaches How to Ru the Drill Five feet
More informationInstructor: Dr. Istadi (http://tekim.undip.ac.id/staf/istadi )
Instructor: Dr. Istadi (http://tekim.undip.ac.id/staf/istadi ) Email: istadi@undip.ac.id Course Syllabus: (Part 1) 1. Definitions of Natural Gas, Gas Reservoir, Gas Drilling and Gas production (Pengertian
More informationPRE LABORATORY ASSIGNMENT: Lab Section Score: /10 READ THE LAB TEXT BEFORE ATTEMPTING THESE PROBLEMS!
EXPERIMENT # 6 Name: PRE LABORATORY ASSIGNMENT: Lab Section Score: /10 READ THE LAB TEXT BEFORE ATTEMPTING THESE PROBLEMS! 1. Calculate the height of a corresponding column of mercury (in mm) that is at
More informationSPH4U Transmission of Waves in One and Two Dimensions LoRusso
Waves travelig travellig from oe medium to aother will exhibit differet characteristics withi each medium. Rules A wave of fixed frequecy will have a shorter wavelegth whe passig from a fast medium to
More informationBasic Gas Spring Theory
Calculatig the iitial force The iitial force of the gas sprig ca be calculated as the sealed area of the pisto rod or the pisto (depedig o desig) multiplied by the pressure iside the gas sprig. The larger
More informationDEPARTMENT OF ELECTRICAL AND COMPUTER ENGINEERING, THE UNIVERSITY OF NEW MEXICO ECE-238L: Computer Logic Design Fall Notes - Chapter 6.
PARTMNT OF LCTRICAL AN COMPUTR NGINRING, TH UNIVRSITY OF NW MXICO C-238L: Computer Logic esig Fall 23 RGISTRS: Notes - Chapter 6 -bit Register: This is a collectio of '' -type flip flops, where each flip
More informationFigure Vapor-liquid equilibrium for a binary mixture. The dashed lines show the equilibrium compositions.
Another way to view this problem is to say that the final volume contains V m 3 of alcohol at 5.93 kpa and 20 C V m 3 of air at 94.07 kpa and 20 C V m 3 of air plus alcohol at 100 kpa and 20 C Thus, the
More information1. A pure substance has a specific volume of 0.08 L/mol at a pressure of 3 atm and 298 K. The substance is most likely:
Name: September 19, 2014 EXAM 1 P a g e 1 1. A pure substance has a specific volume of 0.08 L/mol at a pressure of 3 atm and 298 K. The substance is most likely: a. Liquid b. Gas c. Supercritical Fluid
More informationChem 110 General Principles of Chemistry
CHEM110 Worksheet - Gases Chem 110 General Principles of Chemistry Chapter 9 Gases (pages 337-373) In this chapter we - first contrast gases with liquids and solids and then discuss gas pressure. - review
More informationChapter 13 Gases, Vapors, Liquids, and Solids
Chapter 13 Gases, Vapors, Liquids, and Solids Property is meaning any measurable characteristic of a substance, such as pressure, volume, or temperature, or a characteristic that can be calculated or deduced,
More informationSeries 600 Accessories
Series 600 Geeral These accessories are a rage of devices for completig a peumatic circuit. These valves, with their special fuctios, are iserted betwee two valves, betwee a valve ad a cylider, or followig
More information8.5. Solving Equations II. Goal Solve equations by balancing.
8.5 Solvig Equatios II Goal Solve equatios by balacig. STUDENT BOOK PAGES 268 271 Direct Istructio Prerequisite Skills/Cocepts Solve a equatio by ispectio or systematic trial. Perform operatios usig itegers,
More informationAvailable online at ScienceDirect. Procedia Engineering 113 (2015 )
Available olie at www.sciecedirect.com ScieceDirect rocedia Egieerig 3 (205 ) 30 305 Iteratioal Coferece o Oil ad Gas Egieerig, OGE-205 The twi spool efficiecy cotrol Michuri A.I. a *, Avtoomova I.V. a
More informationIntroduction to Algorithms 6.046J/18.401J/SMA5503
Itroductio to Algorithms 6.046J/8.40J/SMA5503 Lecture 4 Prof. Charles E. Leiserso Quicsort Proposed by C.A.R. Hoare i 962. Divide-ad-coquer algorithm. Sorts i place lie isertio sort, but ot lie merge sort.
More informationChilled Mirror Dew Point Instrument
102 The Relatioship Betee Gas Ad Pressure (SF6) Whe the gas is i the temperature belo the codesig poit, de poit measuremet is ot available This gas codeses o the mirror, the figure belo idicates the relatioship
More informationnumber in a data set adds (or subtracts) that value to measures of center but does not affect measures of spread.
Lesso 3-3 Lesso 3-3 Traslatios of Data Vocabulary ivariat BIG IDEA Addig (or subtractig) the same value to every umber i a data set adds (or subtracts) that value to measures of ceter but does ot affect
More informationSERIES FP4000 FLOW RATES TABLE B** RANGE MODEL RANGE MODEL SERIES FP2000 FLOW RATES TABLE A** RANGE MODEL RANGE MODEL
Data Sheet Field IT Variable Area Flowmeters Acrylic VA Flowmeter Series FP Easy to read Eglish or Metric Scales Water rages from 4CCM to 20GPM Air rages from 50 CCM to 4000 LPM Threaded brass iserts for
More informationBasic Autoclave #1 Ideal Gas Law, Inert Gas
11. Autoclaves 40 Overview An autoclave is a high pressure, high temperature hydrometallurgy unit with carefully controlled conditions. In this chapter, we will simulate an autoclave using two different
More informationUniversity of California, Los Angeles Department of Statistics. Measures of central tendency and variation Data display
Uiversity of Califoria, Los Ageles Departmet of Statistics Statistics 13 Istructor: Nicolas Christou Measures of cetral tedecy Measures of cetral tedecy ad variatio Data display 1. Sample mea: Let x 1,
More informationNatural Gas Desulfurization Process By MEA Amine: The preferable Engineering Design Procedure
Natural Gas Desulfurization Process By MEA Amine: The preferable Engineering Design Procedure Ribwar Abdulrahman 1, Ibtisam Kamal 2, Jagar Ali 3 1 Faculty of Engineering, KoyaUniversity, Kurdistan region,
More informationAbsolute Pressure Gauges: Bellow Type
Absolute Pressure Gauges: Bellow Type MODEL : APBL Why Absolute Pressure Gauge? The atmospheric pressure varies from place to place depedig up o the altitude of the locatio ad prevailig weather coditios.
More informationPROPERTIES OF GASES. [MH5; Ch 5, (only)]
PROPERTIES OF GASES [MH5; Ch 5, 5.1-5.5 (only)] FEATURES OF A GAS Molecules in a gas are a long way apart (under normal conditions). Molecules in a gas are in rapid motion in all directions. The forces
More informationGAS LAW WORKSHEET 1 KEY
377 GAS LAW WORKSHEET 1 KEY 1. A sample of oxygen gas occupies a volume of 436. ml at 1.0 atm. If the temperature is held constant, what would the pressure of this gas be when the gas is compressed to
More informationSPEED OF SOUND MEASUREMENTS IN GAS-MIXTURES AT VARYING COMPOSITION USING AN ULTRASONIC GAS FLOW METER WITH SILICON BASED TRANSDUCERS
SPEED OF SOUND MEASUREMENTS IN GAS-MIXTURES AT VARYING COMPOSITION USING AN ULTRASONIC GAS FLOW METER WITH SILICON BASED TRANSDUCERS Torbjör Löfqvist, Kęstutis Sokas, Jerker Delsig EISLAB, Departmet of
More informationSELECTIVE AMINE TREATING USING TRAYS, STRUCTURED PACKING, AND RANDOM PACKING
SELECTIVE AMINE TREATING USING TRAYS, STRUCTURED PACKING, AND RANDOM PACKING Ralph H. Weiland*, Biliana Oettler**, Christoph Ender***, John C. Dingman**** * Koch-Glitsch, Inc., Dallas, TX, USA ** Koch-Glitsch
More informationDFC NIST DIGITAL MASS FLOW CONTROLLERS. DFC with optional LCD readout PROG RS485. Programmable Mass Flow Controller with Digital Signal Processing
Programmable Mass Flow Cotroller with Digital Sigal Processig Microprocessor drive digital flow cotrollers allow oe to program, record, ad aalyze flow rates of various gases with a computer via a RS-485
More informationIntersleek Pro. Divers Manual. Our World is Water CONTENTS
Itersleek Pro Divers Maual CONTENTS Itroductio.......................................2 Expectatios for Itersleek Pro........................3 I-Water Maiteace...............................4 Haulig the
More informationTHE SOLUBILITY OF HYDROCARBONS IN AMINE SOLUTIONS Supplemental Material
THE SOLUBILITY OF HYDROCARBONS IN AMINE SOLUTIONS Supplemental Material John J. Carroll and James Maddocks Gas Liquids Engineering #3, 279-39th Avenue NE Calgary, Alberta, Canada T1Y T and Alan E. Mather
More informationSlide 1. Slide 2. Slide 3 What do YOU know about oxygen? Dissolved Oxygen. Oxygen. I can t breath in the water but the fish can!
Slide 1 Dissolved Oxygen I can t breath in the water but the fish can! Slide 2 Oxygen Oxygen is one of the fundamental resources required by life forms on Earth. Aquatic ecosystems have a wide assortment
More informationHeadfirst Entry - Diving and Sliding
5/31/2011 Safe divig board use, safe slide use, usi Headfirst Etry - Divig ad Slidig POOLALARMS.COM HOME POOL SAFETY PRODUCTS POOL SAFETY ARTICLES & REPORTS POOL SAFETY LINKS & RESOURCES POOLALARMS.COM
More informationPETROLEUM ENGINEERING 310 FIRST EXAM. September 22, 2000
Session: Name: PETROLEUM ENGINEERING 310 FIRST EXAM September 22, 2000 Do all your work on the test paper and the space provided for the answer, do no write on the back. Grading will be based on approach
More informationHYDROCARBONS AND BTEX PICKUP AND CONTROL FROM AMINE SYSTEMS ABSTRACT
HYDROCARBONS AND BTEX PICKUP AND CONTROL FROM AMINE SYSTEMS Jerry A. Bullin William G. Brown Bryan Research & Engineering, Inc. Bryan, Texas, U.S.A. ABSTRACT HC and BTEX absorption into amine solutions
More informationDate: Period: Gas Laws Worksheet #1 - Boyle s, Charles, Gay-Lussac s, and Combined Gas Law
Name: Date: Period: Gas Laws Worksheet #1 - Boyle s, Charles, Gay-Lussac s, and Combined Gas Law Boyle s Law: V1P1 = V2P2 1. A gas sample contained in a cylinder equipped with a moveable piston occupied
More informationColumn Design Using Mass Transfer Rate Simulation
Column Design Using Mass Transfer Rate Simulation by Ralph H. Weiland and John C. Dingman Optimized Gas Treating, Inc, 15638 Whitewater Lane Houston, TX 77079, U.S.A. info@ogtrt.com Presented at the 80
More informationGas Laws. Figure 1: Experimental Set-up with Leveling Bulb. GCC CHM 151LL: Gas Laws GCC, 2019 page 1 of 8
Gas Laws Introduction Although we cannot see gases, we can observe their behavior and study their properties. This lab will apply several concepts from Ideal Gas Laws. You will use your knowledge of chemical
More informationMATERIAL SAFETY DATA SHEET. 50 BELVER AVENUE CHEMTREC NORTH KINGSTOWN, RI ext. 4501
Polyester film Lumirror ; A53, F65, F7S, F7R, TA30, TA31, U50, U60, U65, U80, UF65, F53, FA6 Page 1 of 5 (Base SDS for Polyester film which is aluminized and crinkled to become insulation.) SECTIO 1 CHEMICAL
More informationPractice MC Test unit D (Ch 10) Gas Laws (pg 1 of 10)
Practice MC Test unit D (Ch 10) Gas Laws (pg 1 of 10) This is practice - Do NOT cheat yourself of finding out what you are capable of doing. Be sure you follow the testing conditions outlined below. DO
More informationWhisperFit EZ Ventilation Fans
FV-08-11VF5, FV-08-11VFM5, FV-08-11VFL5 FV-08-11VF5 FV-08-11VFM5 FV-08-11VFL5 (with 3" duct adapter) Ideal for remodelig ad hotel ew costructio or reovatio Pick-A-Flow Speed Selector oe fa, you choose
More informationChapter 7 Single Point Calculations
Chapter 7 Single Point Calculations Objectives By this point we have learned a great deal about the thermodynamics of the OLI Software and the internal workings of the simulation engine. We have also learned
More informationCHEM254 #4 The Synthesis of a Tertiary Alcohol Using a Pre-Made Grignard Reagent 1
CHEM254 #4 The Synthesis of a Tertiary Alcohol Using a Pre-Made Grignard Reagent 1 Background In this project, we will perform a Grignard reaction using a pre-made Grignard reagent. Grignard reagents can
More informationExample 5.1 Converting between Pressure Units
Example 5.1 Converting between Pressure Units For Practice 5.1 Your local weather report announces that the barometric pressure is 30.44 in Hg. Convert this pressure to psi. For More Practice 5.1 Convert
More informationDetermination of Dissolved Gases in Ground Waters. By Ray Martrano Laboratory Director Seewald Laboratories Inc.
Determination of Dissolved Gases in Ground Waters By Ray Martrano Laboratory Director Seewald Laboratories Inc. Overview of Presentation What is a dissolved gas? Why do we want to study dissolved gases?
More informationTHE EFFECTS OF COUPLED INDUCTORS IN PARALLEL INTERLEAVED BUCK CONVERTERS
THE EFFECTS OF COUPED INDUCTORS IN PARAE INTEREAVED BUCK CONVERTERS Paul Seria, David Fi ad Geoff Walker pseria@itee.uq.edu.au School of Iformatio Techology ad Electrical Egieerig Uiversity of Queeslad
More informationSYMMETRY AND VARIABILITY OF VERTICAL GROUND REACTION FORCE AND CENTER OF PRESSURE IN ABLE-BODIED GAIT
SYMMETRY AND VARIABILITY OF VERTICAL GROUND REACTION FORCE AND CENTER OF PRESSURE IN ABLE-BODIED GAIT Yu Wag ad Kazuhiko Wataabe Graduate School of Educatio, Hiroshima Uiversity, Hiroshima, Japa, wagyu@hiroshima-u.ac.jp
More information16. Studio ScaleChem Calculations
16. Studio ScaleChem Calculations Calculations Overview Calculations: Adding a new brine sample Studio ScaleChem can be used to calculate scaling at one or more user specified temperatures and pressures.
More informationComputer Architecture ELEC3441
Computer rchitecture ELEC344 ISC vs CISC Iro Law CPUTime = # of istructio program # of cycle istructio cycle Lecture 5 Pipeliig () Dr. Hayde Kwok-Hay So Departmet of Electrical ad Electroic Egieerig L4
More informationM3P. Safety Data Sheet TABLE OF CONTENTS IDENTIFICATION OF THE SUBSTANCE/MIXTURE AND OF THE COMPANY/UNDERTAKING 2 SECTION 2 HAZARDS IDENTIFICATION 2
Accordig to the Hazard Commuicatio Stadard (CFR29 1910.1200) HazCom 2015 TABLE OF CONTENTS SECTION 1 IDENTIFICATION OF THE SUBSTANCE/MIXTURE AND OF THE COMPANY/UNDERTAKING 2 SECTION 2 HAZARDS IDENTIFICATION
More informationChemistry 101 Chapter 5 GAS MIXTURES
GAS MIXTURES Consider mixing equal volumes of 3 different gases, all at the same temperature and pressure in a container of the same size. 1 L He 1 L N 2 1 L O 2 1 L mixture t = 0 0 C t = 0 0 C t = 0 0
More informationCHEMISTRY - CLUTCH CH.5 - GASES.
!! www.clutchprep.com CONCEPT: UNITS OF PRESSURE Pressure is defined as the force exerted per unit of surface area. Pressure = Force Area The SI unit for Pressure is the, which has the units of. The SI
More information1. Quantity of a gas (moles) 2. Temperature of the gas. 3. Volume occupied by the gas. 4. Pressure exerted by the gas. PV = nrt
Experiment 5 Stoichiometry : Gases Determining the Ideal Gas Constant Lab Owl Announcement: Upon completion of this lab log onto OWL. Your fourth Lab Owl assignment, Lab Owl: Exp 5 should appear there.
More informationDAMAGE ASSESSMENT OF FIBRE ROPES FOR OFFSHORE MOORING
RECOMMENDED PRACTICE DNV-RP-E304 DAMAGE ASSESSMENT OF FIBRE ROPES FOR OFFSHORE MOORING APRIL 2005 FOREWORD (DNV) is a autoomous ad idepedet foudatio with the objectives of safeguardig life, property ad
More informationWelcome to the world of the Rube Goldberg!
Welcome to the world of the Rube Goldberg! Sice 1988, tes of thousads of studets have competed i our aual Rube Goldberg Machie Cotests where they are challeged to build the wackiest workig Rube Goldberg
More informationCatenary Analysis and Calculation Method of Track Rope of Cargo Cableway with Multiple Loads
MATEC Web of Cofereces 8, 01008 (016) DOI: 10.1051/ mateccof/016801008 DME 016 Cateary Aalysis ad Calculatio Method of Track Rope of Cargo Cableway with Multiple Loads Jia Qi a, Ju Che, Liag Qiao, Jiacheg
More informationExample: Calculate the density of methane at 50 psig and 32 ⁰F. H.W. In previous example calculate the density of methane in gm/m 3.
Gas density Because the density of a substance is defined as mass per unit volume, the density of gas (ρ g ), at given temperature and pressure can be derived as follows: If P in psia, T in ⁰R and R =
More informationAutoclave Calculations
Autoclave Calculations Introduction An autoclave is a high pressure, high temperature hydrometallurgy unit with carefully controlled conditions. From an OLI Software perspective, it is an isochoric (constant
More informationCoal Pulveriser. Global Solutions
Coal Pulveriser. Global Solutios > Worm Gears > Gear Uits > Coupligs & Freewheels Global Coal Pulveriser Solutios Reold is a global egieerig group with over 130 years of experiece i the desig ad maufacture
More informationInternational key comparison
Iteratioal key compariso COOMET.QM-K76 (COOMET project 484/RU/09) KEY COMPARISON OF PRIMARY STANDARD GAS MIXTURES: SO i Nitroge (100 μmol/mol) Sait-Petersburg 013 1 Fial report L.A. Koopelko 1, Y.A. Kustikov
More informationGenerating Calibration Gas Standards
Technical Note 1001 Metronics Inc. Generating Calibration Gas Standards with Dynacal Permeation Devices Permeation devices provide an excellent method of producing known gas concentrations in the PPM and
More informationGFC NIST MASS FLOW CONTROLLERS. Typical Stainless Steel GFC Mass Flow Controller. Design Features. General Description. Principles of Operation
Model thermal Mass Flow Cotrollers are desiged to idicate ad cotrol set flow rates of gases. The combies the characteristics ad accuracy of covetioal mass flow devices ito a uique compact desig at low
More informationGFC NIST MASS FLOW CONTROLLERS. Typical Stainless Steel GFC Mass Flow Controller. Design Features. General Description. Principles of Operation
BULLETIN EM20180402 Model thermal Mass Flow Cotrollers are desiged to idicate ad cotrol set flow rates of gases. The combies the characteristics ad accuracy of covetioal mass flow devices ito a uique compact
More information-H- Note. Flow control valve. Key features
Flow cotrol valves Flow cotrol valves Key features Fuctio Flow cotrol or oe-way flow cotrol valves regulate the pisto speed of peumatic drives durig advace ad retur strokes. This is doe through suitable
More information"The twisting movement of any hoof should, for physiological reasons, not be hindered by Shoeing." (Lungwitz 1884)
Volume 15: Issue 2 Shoeig for Rotatioal Deviatio of the Equie Limb by Michael J. Wildestei CJF, FWCF (Hos) Examiatio of a horse prelimiary to shoeig should be made while the aimal is at rest ad afterwards
More informationASTM 3612/TOGA/Dissolved Gas GC Revised October 2013
The SRI ASTM 3612/TOGA/ Dissolved Gas GC configuration ( TOGA GC ) permits measurement of gasses dissolved in water, oil or other liquids, and is based on the requirements of ASTM method 3612, option C,
More informationPatrick Boston (Leeds University) and Mark Chapman (Edinburgh University)
Iversio o requecy-depedet AVO data or luid properties Patric Bosto (Leeds Uiversity) ad Mar Chapma (Ediburgh Uiversity) Summary A umber o methods to estimate the requecy-depedece o relectivity have bee
More informationChemistry 1B Chapter 10 Worksheet - Daley. Name
Name 1) The National Weather Service routinely supplies atmospheric pressure data to help pilots set their altimeters. The units the NWS uses for atmospheric pressure are inches of mercury. A barometric
More informationUnit 10: Gas Laws. Monday Tuesday Wednesday Thursday Friday. 10 Review for Cumulative Retest. 17 Chem Think Gas Laws Tutorial- Computer Lab-
Unit 10: Gas Laws Name: Monday Tuesday Wednesday Thursday Friday February 8 Stoichiometry Test Review 9 Stoichiometry Test 10 Review for Cumulative Retest 11 Cumulative Re-Test 12 Pressure & Kinetic Theory
More informationHow is pressure handled when we have a mixture of gases?
Name Chem 161, Section: Group Number: ALE 23. Mixtures of Gases (Reference: Chapter 5 in Silberberg 5 th edition) How is pressure handled when we have a mixture of gases? The Model: Collecting Gas Over
More informationCity of Valdez REQUEST FOR QUOTES. Project Name: Lowe River Levee Certification Groin 1 Freeboard Repairs PO Number: Cost Code:
---July 19, 2017--- Dear Contractor: City of Valdez REQUEST FOR QUOTES Project ame: Lowe River Levee Certification Groin 1 Freeboard Repairs PO umber: 74818 Cost Code: 30-070-000 This project includes,
More informationYou should be able to: Describe Equipment Barometer Manometer. 5.1 Pressure Read and outline 5.1 Define Barometer
A P CHEMISTRY - Unit 5: Gases Unit 5: Gases Gases are distinguished from other forms of matter, not only by their power of indefinite expansion so as to fill any vessel, however large, and by the great
More informationName Hour. The Behavior of Gases. Practice B
Name Hour The Behavior of Gases Practice B B 1 Objective 1: Apply Boyle s Law, Charles s Law, and Gay-Lussac s Law to solve problems involving pressure and volume and temperature. 1. A high-altitude balloon
More informationP h o t o g r a p h i c L i g h t i n g ( 1 1 B )
9 1 5 9 P h o t o g r a p h i c L i g h t i g ( 1 1 B ) 30S/30E/30M A Photography Course 9 1 5 9 : P h o t o g r a p h i c L i g h t i g ( 1 1 B ) 3 0 S / 3 0 E / 3 0 M Course Descriptio This course focuses
More informationSCH3U7 Quantitative Chemistry
SCH3U7 Quantitative Chemistry So far, we have looked at solids and liquids (solutions) Today we will look at gases and the laws that govern their behaviour in chemical reactions 4 Factors Affecting Gases
More informationChapter 12. The Gaseous State of Matter
Chapter 12 The Gaseous State of Matter The air in a hot air balloon expands When it is heated. Some of the air escapes from the top of the balloon, lowering the air density inside the balloon, making the
More informationWATER VALVES REPLACEMENT PROJECT
WATER VALVES REPLACEMET PROJECT BROWSVILLE, TEXAS BID o B026-17 PUBLIC B R O W S V I L L E UTILITIES B OARD Brownsville - Board of Directors RAFAEL VELA...CHAIR RAFAEL S. CHACO...VICE-CHAIR MARTI C. ARAMBULA...SECRETARY/TREASURER
More informationINTEROFFICE MEMORANDUM MODIFICATIONS TO DEW POINT CONTROL PROCESS
INTEROFFICE MEMORANDUM TO: FROM: SUBJECT: NEW ENGINEER I.M. ANOLDGUY MODIFICATIONS TO DEW POINT CONTROL PROCESS DATE: JANUARY 10, 2017 We are looking to make modifications to our initial design for a DPC
More informationPURE SUBSTANCE. Nitrogen and gaseous air are pure substances.
CLASS Third Units PURE SUBSTANCE Pure substance: A substance that has a fixed chemical composition throughout. Air is a mixture of several gases, but it is considered to be a pure substance. Nitrogen and
More informationDetermination of the Percentage Oxygen in Air
CHEM 121L General Chemistry Laboratory Revision 1.2 Determination of the Percentage Oxygen in Air In this laboratory exercise we will determine the percentage by volume of Oxygen in Air. We will do this
More informationExperiment 12: MOLAR VOLUME OF AN IDEAL GAS
Experiment 1: MOLAR VOLUME OF AN IDEAL GAS Purpose: Determine the molar volume of a gas at standard temperature and pressure (STP, 0 C and pressure of 1 atm) Performance Goals: Collect and measure the
More informationMaterial Safety Data Sheet
Material Safety Data Sheet PRODUCT AME: IDETIFICATIO AD DISTRIBUTOR IFORMATIO TRADE AME: CAS #: 67701-06-8 EIECS#: 2669306 DATE: DISTRIBUTOR: ADDRESS: ACME-HARDESTY COMPAY 450 Sentry Parkway Blue Bell,
More informationInstructor s t Background
Teknologi Pemrosesan Gas (TKK 564) Instructor: Dr. Istadi (http://tekim.undip.ac.id/staf/istadi ) Email: il iistadi@undip.ac.id di di id Instructor s t Background BEng. (1995): Universitas Diponegoro Meng.
More informationAnalysis of Various Flow Schemes for Sweetening with Amines
Page 1 of 16 Analysis of Various Flow Schemes for Sweetening with Amines LILI LYDDON, Bryan Research & Engineering, Inc., Bryan, Texas HUNG NGUYEN, Bryan Research & Engineering, Inc., Bryan, Texas ABSTRACT
More informationsecuring your safety
securig your safety LIFE POINT PRO DEFIBRILLATOR AN AUTOMATED EXTERNAL DEFIBRILLATOR (AED) CAN BE THE DIFFERENCE BETWEEN LIFE AND DEATH. Statistics show that early 200,000 people die each year as a result
More informationConsiderations for Sampling Wet, High Pressure, and Supercritical Natural Gas. Presented by: Shannon M. Bromley
Considerations for Sampling Wet, High Pressure, and Supercritical Natural Gas Presented by: Shannon M. Bromley Introduction The key to analyzer performance and accurate analysis is proper sample conditioning
More informationA SECOND SOLUTION FOR THE RHIND PAPYRUS UNIT FRACTION DECOMPOSITIONS
Fudametal Joural of Mathematics ad Mathematical Scieces Vol., Issue, 0, Pages -55 This paper is available olie at http://www.frdit.com/ Published olie November 9, 0 A SECOND SOLUTION FOR THE RHIND PAPYRUS
More informationEQUIPEX NAOS WP5 : Deep oxygen floats in the North- Atlantic
EQUIPEX NAOS WP5 : Deep oxyge floats i the North- Atlatic Virgiie Thierry Guillaume Maze, Herlé Mercier, Cécile Cabaes, Virgiie Racapé Laboratoire d Océaographie Physique et Spatiale UMR 6523 CNRS / IFREMER
More informationGases NO CALCULATORS MAY BE USED FOR THESE QUESTIONS
NO CALCULATORS MAY BE USED FOR THESE QUESTIONS Questions 1-3 refer to the following gases at 0 C and 1 atm. (A) Ar (B) NO 2 (C) Xe (D) H 2 (E) N 2 1. Has an average atomic or molecular speed closest to
More informationFunsheet [WHAT IS PRESSURE AND TEMPERATURE] Gu 2015
Funsheet 7.0 7.1 [WHAT IS PRESSURE AND TEMPERATURE] Gu 2015 1. Convert the following pressures. a) 101 kpa =? atm b) 55 Torr =? psi c) 60. mmhg =? bar d) 45 Torr =? kpa e) 5 psi =? atm f) 0.0056 atm =?
More informationChapter 13 Gases and Pressure. Pressure and Force. Pressure is the force per unit area on a surface. Force Area. Pressure =
Chapter 13 Gas Laws Chapter 13 Gases and Pressure Pressure and Force Pressure is the force per unit area on a surface. Pressure = Force Area Chapter 13 Gases and Pressure Gases in the Atmosphere The atmosphere
More informationHeld under the sanction of USA Swimming, issued by North Carolina Swimming, Inc. Sanction No. NC11117
The Greesboro Swimmig Associatio's 2011 Joh Gordo Dewey Ivitatioal Swim Meet November 19-20, 2011 The Greesboro Aquatic Ceter 1921 West Lee Street, Greesboro, NC 27403 SANCTION: HOST: FACILITY: Held uder
More informationCountercurrent Stagewise Operations Equilibrium Stage Number of Actual Stages Definition of The Design Problem...
Countercurrent Stagewise Operations All rights reserved, Armando B. Corripio 2013 Contents Countercurrent Stagewise Operations... 1 1 Equilibrium Stage... 4 1.1 Number of Actual Stages.... 5 2 Definition
More informationXFM DIGITAL MASS FLOW METER. XFM with Profibus Interface. XFM without. Readout. XFM with. Readout. Option
BULLETIN EM20180402 Desig Features Supports up to 23 Egieerig Uits (icludig User Defied). Stores calibratio data for up to 10 gases. Programmable Totalizer idicates total gas quatity. High ad low gas flow
More informationUNIT 10 - GASES. Notes & Worksheets - Honors
Ideal Gas Equation 1 WKSHT 1.) What is the pressure exerted by 2.0 moles of an ideal gas when it occupies a volume of 12.0 L at 373 K? 2.) A flashbulb of volume 2.6 cm 3 contains O 2 gas at a pressure
More informationFDE 211 Material & Energy Balances. Instructor: Dr. Ilgin Paker Yikici Fall 2015
FDE 211 Material & Energy Balances Instructor: Dr. Ilgin Paker Yikici Fall 2015 Material& Energy Balances first step in understanding a process leads to a better understanding of a process forces the engineer
More information2. Calculate the ratio of diffusion rates for carbon monoxide (CO) and carbon dioxide (CO2). υa = MB = 44 = 1.25
Gas laws worksheet (2-08) (modified 3/17) Answer key Graham s Law 1. Calculate the ratio of effusion rates for nitrogen (N2) and neon (Ne). υa = MB = 20 = 0.845 υb MA 28 2. Calculate the ratio of diffusion
More informationLoad Calculation and Design of Roller Crowning of Truck Hub Bearing
Sed Orders for Reprits to reprits@bethamsciece.ae 106 The Ope Mechaical Egieerig Joural, 2015, 9, 106-110 Ope Access Load Calculatio ad Desig of Roller Crowig of Truck Hub Bearig Xitao Xia,1, Shujig Dog
More information