Accelerating Rate Calorimeter

Similar documents
APTAC Test Procedure for DIERS Round Robin Testing of Vinyl Acetate Polymerization

The HumiPyc - Model 1 - Gas Pycnometer; Density, Moisture, Permeation Analyzer; RH sensor Calibrator

CONTROL and OPERATIONS

Major Design Features

Application Note AN-107

High Pressure Chem-SCAN Operating Manual

AC : MEASUREMENT OF HYDROGEN IN HELIUM FLOW

Series Environmental Chambers

The HumiPyc ( Model 2) - Gas Pycnometer; Density, Moisture, Permeation Analyzer; Filter Integrity Tester; RH sensor Calibrator

Chemistry - Scale-up F.32. Lara TM - Controlled - Lab Reactor. The Concept

Adiabatic Calorimetry

BAROMETER PRESSURE STANDARD PRESSURE CONTROLLER

Schedule of Requirements THERMODYNAMICS LABORATORY- CHEMICAL ENGINEERING DEPARTMENT

Title: Standard Operating Procedure for R&R Environmental Devices Model MFC201 Gas Dilution Calibrator

L 100. Bubble-Tube Level System. Installation, Operation and Maintenance Instructions

Experiment. THE RELATIONSHIP BETWEEN VOLUME AND TEMPERATURE, i.e.,charles Law. By Dale A. Hammond, PhD, Brigham Young University Hawaii

The HumiSys. RH Generator. Operation. Applications. Designed, built, and supported by InstruQuest Inc.

Relief Systems. 11/6/ Fall

Lab 1c Isentropic Blow-down Process and Discharge Coefficient

AUTOMATIC HOSE TEST UNIT, TYPE SPU

IDeA Competition Report. Electronic Swimming Coach (ESC) for. Athletes who are Visually Impaired

Low gas volume & flow measurements made easier Gas Endeavour

bespoke In general health and rehabilitation Breath-by-breath multi-functional respiratory gas analyser In human performance

Variable Temperature Operation

PRC CO ² -LASER PRESENTATION

FPG8601 Force Balanced Piston Gauge

Relief System Sizing for Runaway Chemical Reactions: A Simple Comprehensive Approach

THE PMI AUTOMATED GAS/HELIUM PYCNOMETER PYC-G100A

H 2 O Bubble Chamber Superheated Active Target System. Safety and Systems Overview B. DiGiovine

FAST EVAPORATION AT NORMAL PRESSURE

Oxidation Stability of Gasoline and Aviation Fuels

Qi Litre Ultrasonic Cleaner

Armfield Distillation Column Operation Guidelines

Cryostream 800 Series

SF 6 Product Guide. Gas Analysis Instruments and Accessories

Pneumatic high-pressure controller Model CPC7000

FTS SUBMERSIBLE PRESSURE TRANSMITTER USER S MANUAL

UNITY 2 TM. Air Server Series 2 Operators Manual. Version 1.0. February 2008

CHE 4115 Chemical Processes Laboratory 2 Experiment 1. Batch Distillation

ACCURATE PRESSURE MEASUREMENT FOR STEAM TURBINE PERFORMANCE TESTING

Agilent Flowmeter ADM1000

CONTROL and INSTRUMENTATION

Automated Determination of Dissolved Gases in Water By Headspace Calibration of Mixed Gases Anne Jurek

Rheological properties. Rheological instruments backed with rheological experience. Malvern. detailed specification sheets from

These Terms and conditions apply to audit trails incorporated in weighing and measuring devices and systems 1.

Pneumator. Testo Industrial Services More assurance, better service. Pressure calibrator and measuring instrument.

2600T Series Pressure Transmitter Models 264DC Differential and 264HC Gage Level Transmitters. Kent-Taylor

Hot extractive multi-channel gas analyser for continuous process and emissions monitoring.

Vibration-Free Joule-Thomson Cryocoolers for Distributed Microcooling

Automated Determination of Dissolved Gases in Water Anne Jurek. Abstract: Discussion:

SSI Solaris 150 RTA Revision /27/2016 Page 1 of 9. SSI Solaris 150 RTA

Technical Specifications of Hydrogen Isotope Handling and Recovery System

A Depletion Compensated Wet Bath Simulator For Calibrating Evidential Breath Alcohol Analyzers

Proudly serving laboratories worldwide since 1979 CALL for Refurbished & Certified Lab Equipment Varian 310

Model 601CV. Mass Flow Controller. Product Features:

How to specify a product. Process Sensors and Mechanical Instruments

Specific Accreditation Criteria Calibration ISO IEC Annex. Mass and related quantities

BUYER S GUIDE AQUAlogger 530WTD

deltaflowc deltaflowc Venturi or Probe

I. CHEM. E. SYMPOSIUM SERIES NO. 85

Physical explosion analysis in heat exchanger network design

c) Loss of product or replacement when units are being serviced All of these are factors that need to be considered by the user.

A NEW PROCESS FOR IMPROVED LIQUEFACTION EFFICIENCY

Pneumatic high-pressure controller Model CPC7000

LEAP CO 2 Laboratory CO 2 mixtures test facility

This test shall be carried out on all vehicles equipped with open type traction batteries.

Prof AH Basson, Pr Eng March Departement Meganiese en Megatroniese Ingenieurswese. Department of Mechanical and Mechatronic Engineering

Oxford Instruments Plasma Technology. PlasmaPro NGP80. Installation Data Sheet. Original Instructions.

Importance of Wave Height Measurement in Wave Solder Process Control

ZIN Technologies PHi Engineering Support. PHi-RPT CFD Analysis of Large Bubble Mixing. June 26, 2006

Tensiometer For the measurement of surface and interfacial tension

Hot extractive multi-channel gas analyser for continuous process and emissions monitoring.

LUMAZOTE T ECHNICAL BRO CHU RE

Kube Engineering Quinn E. Eddins, B.S.E.E Phone

Gas Network Craftsperson

This multi-functional device allows the determination of up to six quality parameters with only one measurement:

OMCL Network of the Council of Europe QUALITY ASSURANCE DOCUMENT

Two-Wire In Situ Oxygen Analyzer (550 to 1400 C)

better measurement Simply a question of SCHMIDT Flow Sensor SS The cost-effective alternative in pressurised systems up to 10 bars.

HumiSys HF High Flow RH Generator

PHOENIX L300i Best-in-class Helium Leak Detectors

BGA244 Binary Gas Analyzer

PART 5 - OPTIONS CONTENTS 5.1 SYSTEM EXPANSION 5-3

TIGHTNESS. Glass sealing Thanks to our glass-sealing technology, ODU products can meet the most demanding tightness requirements.

LFE OEM TCD - Thermal Conductivity Detector

Analysis of Pressure Rise During Internal Arc Faults in Switchgear

Analogue and Digital Mass Flow Meters and Controllers for Gases MASS-STREAM

CO, NO, NO 2, NO x, SO 2, CH 4, HCl, CO 2 & H ² O. Extractive low cost, low maintenance devices for continuous process and emissions monitoring.

HIGH ACCURACY MULTI-GAS MONITORING USING AUTOMATED SELF- CALIBRATION

Discovery HP-TGA 75/750. Site Preparation Guide

Capillary Flow Porometer/Frazier/C-522 CFP-1100AEX-F-C522

Automated Determination of Dissolved Gases in Water Anne Jurek

ONH836 Series: Oxygen/Nitrogen/Hydrogen by Inert Gas Fusion

Best Practice Guide, Servomex 2700

Determination of Capillary pressure & relative permeability curves

Determining Free-Space Values for ASAP Series Micropore Analyses

PMI ADVANCED AUTOMATED HYDRAULIC PRESSURE LEAK TESTER APCS-H-60K. Not just Products... Solutions!

JT Micro Compressor Test Results

MEGAS 2.0. Gas analysis with direct C-Level Calculation and Bus-Connection. Data sheet

MIL-STD-883G METHOD

Transcription:

The World s Benchmark Adiabatic System The Accelerating Rate is unique for its unparalleled adiabacity, its sensitivity and its sample universality. Coupled to this its ease of use and simple data analysis make it accessible and usable by all THERMAL HAZARDAZARD TECHNOLOGY 1 North House Bond Avenue Bletchley MK1 1SW Phone: 01908 646800 Fax: 01908 645209 Info@thermalhazardtechnology.com

An understanding of the energy release from chemical reactions and the potential for runaway reactions is vitally important in the t chemical industry. When the heat generated by a chemical process is greater than the possible heat removal, the temperature will rise with perhaps catastrophic effect. Most chemical reactions proceed with heat release but the amount of heat release, the rate of release and the temperature of onset are very important parameters. Only in an adiabatic calorimeter can such a runaway reaction be reliably evaluated by simulating what can happen on a large scale by mimicking the worst case zero-heat loss conditions. The Accelerating Rate is the most well known and world's most widely used adiabatic calorimeter and will provide full information on the heat and pressure release showing the potential of a runaway occurring. This will also enable optimum o conditions to be employed to allow inherently safe operation. Only when tests are conducted in a truly adiabatic system it possible to scale-up from the laboratory scale

The system is contained in a metal sphere 2.5cm in diameter, typically of Titanium or Hastelloy C. The sample mass is usually 2-8g but would depend upon the expected energy release and type of sample container (known as a bomb) used. The bomb is attached to the lid section on the calorimeter assembly by a pressure fitting and a pressure line leads to the pressure transducer. A fine thermocouple is attached to the outer surface of the bomb and the lid of the calorimeter then positioned on the base section. The calorimeter has three separate thermal zones. The top (lid section) contains two heaters and a thermocouple, the side zone of the base section contains four heaters and a thermocouple and the bottom zone at the base section contains two heaters and a thermocouple. After set up and connection, the calorimeter is sealed within an explosion proof containment vessel. After defining experimental conditions on the PC, the test can commence. The test conditions are a start and end temperature and choosing the size of heat steps', 'wait time' and detection sensitivity'. The system will firstly heat to the start temperature. To do this, a small heater in the calorimeter, the radiant heater, applies heat. This heats the sample, bomb and it's thermocouple. The calorimeter is cooler and this temperature difference is observed by the three calorimeter thermocouples. The system will then apply power to the calorimeter heaters to minimise the temperature difference. This will continue as the temperature rises to the start temperature. When this start temperature is reached the system will go into a wait period, during this time no heat is provided by the radiant heater. This allows the temperature differences within the calorimeter to be reduced to zero. The calorimeter operates adiabatically allowing the - calorimeter temperature to track sample temperature. This wait period (typically 10-15 minutes) is followed by a seek or search period. Again during this period (typically 20 minutes) no heat is provided by the radiant heater, and any temperature drift, upwards or downwards, is observed. If there is upward temperature drift this is caused by a self-heating reaction. The heatwait-seek procedure, the normal mode of operation of the Accelerating Rate, will continue until an upward temperature drift observes an exothermic reaction, greater than the selected sensitivity (normally 0.01-0.02 C/min). The system automatically switches to the exothermic mode; the system will apply heat to the calorimeter jacket to keep its temperature the same as the bomb/sample. The adiabatic control is the key feature of the Accelerating Rate. The system continues in the exotherm mode until the rate of self-heating is less than the chosen sensitivity, at this stage the heat-wait-seek procedure resumes. When the end temperature is reached (or an end pressure is reached) the test automatically stops and cooling, by compressed air, begins. The aim of the Accelerating Rate is to complete the test to get a full time, temperature, and pressure profile of the exothermic reaction in a safe and controlled manner.

The World s Benchmark Adiabatic has been Re-Engineered Introducing. the Low φ Accelerating Rate Continuity Proven design, same bomb types, same mode of operation Results will be the same as those obtained from older style instruments Enhancement Low Phi (φ =1.05) Fume Extraction Cryogenic operation (Testing from 35 C) True Isothermal Age mode Rapid track option Heat and Gas generation plots, SADT and tnr calculations Network-able Industry standard hardware and software Expansion Vent Size Unit Sample Stirring Unit Sample Dosing Unit.Automated Gas Sampling Unit Gas Scrubbing and Safe Release Unit (manual or automatic Cryogenic unit Battery Safety and Cycling Units see separate brochures to assist scientists and engineers involved with safety and hazard testing and analysis

The Re-Engineered Accelerating Rate First available in 1978, but little changed since, full re-engineering of the Accelerating Rate had been overdue. However with many original systems in use and a worldwide acceptance of the data produced, the first need was for Continuity of the data, but with re-engineering there is the possibility of enhancement and expansion of this proven technology. The re-engineered instrument offered by Thermal Hazard Technology allows for all of these aspects. The original well thought out features have been retained but modern microprocessor technology and computer control have been adopted. Continuity The Thermal Hazard Technology Accelerating Rate operates in the proven heat-wait-seek method and has isothermal capabilities. The calorimeter assembly is of the same proven design and the sample containers commonly available may be used. The performance of the system and its main characteristics remain unaltered and sample data from this instrument mirrors that of the original, thus there is continuity of data. Enhancement The hardware and software components are built to international standards, using recognised platforms. The design is such to allow expansion. In addition, the calorimeter containment vessel is designed to allow for improved access, gas extraction and housing of additional equipment. 60ml containers mean f values to 1.05 are obtained. Software design has a user friendly GUI. Expansion Thermal Hazard Technology Accelerating Rate has therefore been designed to fulfil the requirements of an adiabatic calorimeter system but with the ability for ongoing enhancement and development. Options are available; a Vent Sizing Unit is available to allow low f testing, determination of reaction types and for blow-down tests for the determination of relief vent area. There is samplestirring option, a sample dosing option, a gas collection option and a cryogenic option; there is a gas scrubber system to allow safe removal and disposal of potentially toxic gases.

Unparalleled Adiabaticity Proven adiabatic environment around whole sample, with high precision tracking of exothermic reactions. Exceptional Sensitivity Detection of exotherm from 0.003 C/min selfheating, which may be 100W/tonne. Universality of Sample Sample range, very low energy to very highenergy reactions Sample range, liquids solids salaries residues mixtures gases Sample hazard range, processing, storage, transportation. Easy to Use Internationally recognised technique - set-up time before and after a test of 10-20 minutes. and Simple Data Analysis The data from a standard test is column and row data of time, temperature and pressure. From this raw experimental data the self-heat rate, pressure rate, time to maximum rate and all other data types are generated. The data analysis is semi-automated though may be fully analysed manually if preferred Accelerating Rate data has always been considered straight forward to use and apply and this is also the case the Thermal Hazard Technology software. In addition the data analysis allows for input of reaction vessel information to enable maximum safe temperatures or sizes to be determined. There is provision for other types of data analysis, e.g. SADT determination and an automatic report generator is provided. This and the graphical outputs may be user modified to customise or the change. The data analysis allows for production of quality colour output in slide or transparency format.

Di-Tertiary Butyl Peroxide is the chemical usually chosen to illustrate the data from an adiabatic calorimeter. Results obtained from the Thermal Hazard Technology Accelerating Rate are shown below. The data shown here is for illustrative purposes, it shows what may be obtained from a single Accelerating Rate Calorimetry test. The DTBP test is useful as it clearly shows the performance of the system the accuracy of the data and the ability of the system to operate adiabatically In this test 6g of 20% DTBP (98%) by weight in toluene (99 8%) is used. The bomb is a titanium bomb close to 6g in weight. Starting temperature is 90 C; end temperature 220 C the wait time 15 minutes the heat step 3 C and the onset sensitivity 0.01 C/min. Below and more importantly at temperatures above the exothermic reaction it is possible to see how well calibrated the system is and it can be noted that there is little if any drift. This indicates that there is little if any heat loss from the system - many other calorimeters allow considerable heat loss by refluxing on the cold upper surface of the sample container. Analysis of the exotherm itself can be carried out by determining temperature at which certain self-heat rates occur e.g. 0.1 C/min 0.2 C/min 0.5 C/min etc. These repeat to within 1-2 C. Also important to note is the maximum self-heat rate (though this can change with differences in void volume) the final temperature and the pressure rise. Unlike very many samples DTBP is completely reliable as a standard. The other way to analyse is to perform a thermokinetic analysis; the software can do this. There are very many literature reports of DTBP in toluene heat of decomposition and activation energy. These centre on a heat of reaction near 170KJ/mol and activation energy near 160KJ/ mol. Typically the Accelerating Rate working correctly will reproduce these values to ± 2-3%. Getting such results clearly indicates the quality of the techniques and the correct operation of the system in use.

Real Time Data Plot: This shows the temperature against time for the complete test. In addition to showing the course of the experiment with time, the exothermic reaction temperature and magnitude of the reactions the data both before and after the exothermic reaction can be seen. At low temperature, reactions below the exothermic threshold may be noted and at higher temperatures the calibration accuracy of the instrument can be confirmed. By noting the pressure below the exotherm (and above) any indication of leak can be observed - or it may be that there is pressure generated from a non-exothermic process. (see previous page for examples) Temperature and Pressure Plot: The temperature and pressure data are plotted against time to show the onset of reaction, the magnitude of the reaction and as a comparison it can be seen how much pressure is produced over which reaction or temperature range. It can be noted that much of the time of the reaction is in the first few degrees of temperature rise. (shown right) Self elf-heat Rate Plot: The Self-Heat Rate is a key presentation of the results. The onset of reaction can be seen, as can the size, the magnitude, the complexity and number of reactions. The self-heat rate at any temperature is shown as is the maximum self-heat rate. By knowing the self-heat rate at an operating temperature for instance the amount of cooling required can he determined. By comparing the pressure rate with the self-heat rate further important information about the reaction can he obtained. (shown right)

Self-Heat Rate Analysis: Mathematical analysis of the selfheat rate plot can determine heat of reaction, activation energy and other kinetic parameters. The latter is carried out by an automated curve fitting procedure. With the model result this may be used to back-extrapolate the data to get results below the onset of reaction, including time to maximum rate data from the modelled reaction at low temperatures. Pressure and Pressure Rate Temperature Plots: Pressure may be plotted on linear axes or as logarithm of the pressure against reciprocal temperature (Kelvin). Should the data produce a linear plot on linear axes the pressure rise is that of a non-condensable gas, if the plot is linear on logreciprocal axes the pressure rise is likely to that due to vapour pressure increase. In addition a plot of pressure rate and against temperature rate may be produced, a straight line here indicates a single reaction - when heat is pro- Time to Maximum Rate: After selecting the temperature of maximum rate this important curve may be generated. With knowledge of f, the plot may be corrected to worst case. If the model reaction has been determined the time to maximum rate curve may be generated to lower temperatures. This presentation of data shows immediately the amount of time available from any temperature to runaway, possible disaster - in the worst case. The plot may also be used to determine maximum safe temperatures or size of storage vessels; the data may be used to determine SADT.

Operations Software The Set-up of a test is carried out by entry of information into user-friendly screens. This will include information on the sample and the bomb. All information entered here and data from the test result will link directly to the Microsoft Word Report that can be automatically generated after the test. It is possible to manually override the test conditions and run mode during the test. During the test the screen graphical user interface shows clearly the current status. The software can be networked such that the user can view run information remote from the instrument.

Vent Sizing THT s Unique VSU (Vent Sizing Unit) utilizes DIERS technology to perform: Closed vessel, Tempering, and Blowdown tests. THT have experience in all aspects of process design and safety. The use of modern instrumentation and advanced software modelling allow THT to provide rapid and accurate themal safety assesment. Options and other products from Thermal Hazard Technology: Uniquely THT have developed the Accelerating Rate to extend its operation and usefulness: Low Phi, Vent Sizing, Cryogenic Operation, Sample Gas Collection, Sample Gas Safe Release, Sample Stirring and Dosing. THT have also developed the Battery Safety to allow use and abuse testing to be carried out with 1 instrument. System Specifications: Sample sizes: mg-grams (>50g with low-phi test cell) Phi Range: 1.05 and higher Operating Temperature Range: Ambient - 500 C (absolute max 600 C) (Sub-zero with cryogenic option) Maximum Sensitivity: 0.005 C/min (typical power equivalent 30mW/g) Maximum Isothermal Stability (in Isothermal mode) 0.002 C over 24 hours, onset detection from 0.002 C/min Maximum Heat Rate (in Ramp mode) 10 C/min Pressure Limit 200bar (higher value transducers available) Mains Supply: Voltage: 100, 110, 120, 200, 220, 240 V AC / Frequency: 50, 60 Hz / Power: 2.5 kw Cooling: Dry Air @ 2-10 bar (6 mm ID flexible tube) THERMAL HAZARDAZARD TECHNOLOGY 1 North House Bond Avenue Bletchley MK1 1SW Phone: 01908 646800 Fax: 01908 645209 Info@thermalhazardtechnology.com