Huntsman Corporation Australia Pty Ltd. Botany Site NSW. Environment Protection Licence Reporting Period: to

Similar documents
Frequently Asked Questions Directive 056 Facilities Technical

TECHNICAL AMENDMENT D To INTEGRATED POLLUTION PREVENTION & CONTROL LICENCE

POLLUTION INCIDENT RESPONSE MANAGEMENT PLAN

Permitted MSS Emissions Tracking, Recordkeeping, and Reporting. Presented by ACES April 24, 2008

NOTICE. Issued: February 12, 2010 AO# Dundas Street West, Oakville, ON CANADA Phone: (905) Fax: (905)

Secondary Aluminum NESHAP 40 CFR Part 63 Subpart RRR. Example Malfunction Plan for Plant ABC

A TYPICAL AERATION UPGRADE CONSIDERATIONS AND OUTCOMES. Michael Young. Michael Young, Director, Faraga Pty Ltd and Aer-Force Pty Ltd

F All types of inert gas systems are to comply with the following:

APPENDIX 4 STANDARD FORMAT FOR THE PROCEDURES AND ARRANGEMENTS MANUAL

ANNEX AMENDMENTS TO THE INTERNATIONAL CODE FOR FIRE SAFETY SYSTEMS (FSS CODE) CHAPTER 15 INERT GAS SYSTEMS

Section 1. Registration Information

EXAMPLES OF COMPLIANCE METHODS FOR MONITORING AND RECORDKEEPING RCRA SUBPARTS BB AND CC. Tennessee Operations Eastman Chemical Company

3M Steri-Vac Sterilizer/Aerator GSX Series. For Life Science Applications. Product. Profile

TEMPLE UNIVERSITY ENVIRONMENTAL HEALTH AND RADIATION SAFETY

The Protection of Silos From Over. Pressurisation During Filling

Start-up, Shutdown and Malfunction Plans. Norman L. Morrow Fresh Air Consulting

Waste Management System.

AirSep PSA Nitrogen Systems

Requirements for the Ethylene MACT

Contents. Foreword. Acknowledgements. General Introduction

Tanker Officer Training Standards (TOTS) 4C Product Tanker Simulator Training Course

SLOP RECEPTION AND PROCESSING FACILITIES

RESOLUTION A.567(14) adopted on 20 November 1985 REGULATION FOR INERT GAS SYSTEMS ON CHEMICAL TANKERS

Reduce Turnaround Duration by Eliminating H 2 S from Flare Gas Utilizing VaporLock Scrubber Technology

Subparts AA and BB - The Other RCRA Air Rules. Beginners aabb

Dow s New Practice for Locating Temporary Portable Buildings. P. Partridge 9/29/05 UNRESTRICTED - May be shared with anyone Slide 1

Safe management of industrial steam and hot water boilers A guide for owners, managers and supervisors of boilers, boiler houses and boiler plant

Session One: A Practical Approach to Managing Safety Critical Equipment and Systems in Process Plants

Commandant United States Coast Guard

Minimum standard of competence in advanced training for liquefied gas tanker cargo operations (STCW Reg V/1-2)

EDUCATION DEPARTMENT ACCU-TEST

M-06 Nitrogen Generator (Nitrogen Making Machine)

SWMS No 001 Samark North Qld Pty Ltd ABN : Electrical Contractors License C37121 Page 2 of 5

Active Hydrophore System AHS-01

Dri-Line Mk3 Monnier Compressed Air Drain Trap

RESOLUTION MSC.397(95) (adopted on 11 June 2015) AMENDMENTS TO PART A OF THE SEAFARERS' TRAINING, CERTIFICATION AND WATCHKEEPING (STCW) CODE

General Duty Clause. Section 112(r)(1) of CAA. Chris Rascher, EPA Region 1

Dynamic Simulation for T-9 Storage Tank (Holding Case)

Operational Settings:

HUMAN FACTORS CHECKLIST

Critical Systems Inc. Work Instruction Template. Doc Number: CSI Delatech 6/12 Month PM-003 WORK INSTRUCTION

PSM TRAINING COURSES. Courses can be conducted in multi-languages

Introduction to HAZOP Study. Dr. AA Process Control and Safety Group

STCW Code Table A-V/1-1-1 Specification of minimum standard of competence in basic training for oil and chemical tanker cargo operations

Requirements for Reduced Supervision of Power Plants, Thermal Liquid Heating Systems, and Heating Plants

OIL AND GAS PROCESSES AND EMISSIONS

Bogo Operations Pollution Incident Response Management Plan

PENNSYLVANIA DEPARTMENT OF ENVIRONMENTAL PROTECTION

Decant Filling of Gas Cylinders

Steam System Best Practices 14 Best Practices for Guide Lines for Boiler Plant Log Books

Operating Instructions

A Sub-Synchronous Vibration Problem: Trapped Fluid in Compressor Coupling Spacer. Diagnosis and Resolution

NORMAL OPERATING PROCEDURES Operating Parameter Information

IX1 Spirax-Monnier International Compressed Air Filter Installation and Maintenance Instructions

SYNTHETIC MINOR OPERATING PERMIT

Automatic Isokinetic Sampler. ST5 Evo

"INOGATE Technical Secretariat & Integrated Programme in support of the Baku Initiative and the Eastern Partnership energy objectives" Project

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

TECHNICAL DATA. Q = C v P S

Thermocirc Installation and Maintenance Instructions

TECHNICAL DATA OBSOLETE

TECHNICAL DATA. Q = C v P S

Safety Engineering - Hazard Identification Techniques - M. Jahoda

LEGIONELLA MANAGEMENT PROCEDURE

Flare Gas Composition Analysis and QA/QC Lessons Learned and Lessons Lost SPECTRUM ENVIRONMENTAL SOLUTIONS, LLC 1

Hazardous Materials Management Guidelines

System Pressure Manager Standard & System Pressure Manager Plus

NZQA registered unit standard version 3 Page 1 of 8. Operate bitumen gangbar sprayer transfer, heating, and blending equipment

NZQA registered unit standard version 3 Page 1 of 7. Demonstrate knowledge of bitumen gangbar sprayers and operations

What is LPG? Released Energy in the narrowest area. Clean and sure in the practise

Gianluca Gemme LN2 DISTRIBUTION PLANT

RECOMMENDED GOOD PRACTICE

ANTI-ENTRAPMENT PLAN

QuickHeat TM Packaged Heat Exchanger Solutions

INSPECTION OF MEDICINAL GASES

Analysis of Pressure Rise During Internal Arc Faults in Switchgear

TECHNICAL DATA. the Viking Pilot Pressure Regulating Valve 1 Model A-1 Speed Control Assembly: OBSOLETE. the Viking Speed Control Assembly 1

Edge Isolation Tool. Standard Operating Procedure. Version 1.1. Date: Prepared by, Sandeep S S. Department of Electrical Engineering

TECHNICAL DATA Q= C. Table 1 - Specifications

Standard for Hazardous Waste Management, Compliance Checklist. Sean K. Grady, CHMM Vice President-Principal

Risk Analysis- Sulfuric Acid

1. UPDATE 12/12/2014: What wells are regulated under the MIA Program? Must they be drilled, stimulated, and completed? Must they be in production?

Usage Policies Notebook for Trion RIE / ICP Dry Etch

3. Possession or use of weapon unlawful to extent another licence is needed to authorise that possession or use

USE A RELIABLE A INNOVATIVE A COST EFFICIENT GAS EQUIPMENTS AND GAS SYSTEMS

MFP14-PPU (Vented) Automatic Packaged Pump Units

Procedure: Pressure equipment safety

NSPS SUBPART Ka Check-off Form JULY 11, LAFAYETTE ROAD NO., ST. PAUL, MN

Air Eliminators and Combination Air Eliminators Strainers

TECHNICAL DATA. Table 1 - Specifications

TECHNICAL DATA. Q = C v P S

TECHNICAL DATA. Q = C v P S

REDUCING EMISSIONS WHEN TAKING COMPRESSORS OFF-LINE

Flexibility Enhancements for Gas Turbines

Automatic Isokinetic Sampler. ST5 Evo

Portable Oil Lube Air Compressors

Example Report. EXAMPLE How to perform. infrared trending of Electric Motors. Plant Air Wash Supply Fan. Temperature Rise = High Temp = Ambient =

CONGRATULATIONS ON YOUR PURCHASE OF YOUR THUNDER COMPRESSOR For your personal safety please read, understand and follow the information provided in

Little Spokane River Stream Gage Report: Deadman Creek, Dragoon Creek, and the West Branch of the Little Spokane River

FUNDAMENTAL SAFETY OVERVIEW VOLUME 2: DESIGN AND SAFETY CHAPTER I: AUXILIARY SYSTEMS. A high-capacity EBA system [CSVS] [main purge]

Transcription:

Huntsman Corporation Australia Pty Ltd Botany Site NSW Environment Protection Licence 7494 Reporting Period: 23-12-2015 to 22-12-2016 Vent Management System Annual Report 2016 A. Company and site details Company Name Huntsman Corporation Australia Pty Ltd Company Site Address 77 Denison Street Hillsdale NSW 2036 (Botany Industrial Park) Environment Protection Licence No. 7494 NSW EPA Website Link NSW Environment Protection Authority (EPA) B. Monitoring point details Monitoring Requirement Monitoring Point Number 1 2 3 Description Discharge to atmosphere from Vent Management System (VMS) scrubbing column Flowrate of VMS scrubbing liquor measured by FI 19308 (flow indicator) Conductivity of VMS scrubbing liquor measured by CI 19309 (conductivity indicator) Frequency Annual Continuous Continuous Pollutant Ethylene oxide Propylene oxide - - Unit kg/ hour cubic metres/ hour (m 3 /hr) millisiemens/ centimetre (ms/cm) Lower Limit - - 24 80 Upper Limit 0.22 6.05 - - Averaging Period 1 hour 1 hour - - Plant Conditions during Monitoring 1 Ethylene oxide storage tanks must be venting to the VMS Propylene oxide road tanker must be unloading to storage tank - - Note 1: The mass emission rates that are measured during the VMS Annual Test are representative of emission rates under an infrequent peak loading situation and are not representative of the emission rates that occur for the majority of the time.

C. Monitoring results for 2016 Monitoring Results Date data obtained Monitoring Point Number 1 2 3 17 th August 2016 January 2016 December 2016 Pollutant Ethylene oxide Propylene oxide - - Unit kg/ hour cubic metres/ hour millisiemens/ centimetre Results (i) < 0.000001 < 0.000001 Plant Conditions during Monitoring Propylene oxide tanker unloading to storage tank, Ethylene oxide storage venting to VMS See charts below (ii) < 0.0000004 < 0.000001 Plant Conditions during Monitoring Propylene oxide tanker venting down, Ethylene oxide storage venting to VMS Monitoring Point 1 Results from the sampling at Monitoring Point 1 complied with the upper limit requirement. The results were below the limit of measurement for the instrumentation. Monitoring Points 2 and 3 The charts below show the results for continuous monitoring at Monitoring Points 2 and 3 of the VMS for 2015. Monitoring Point 2: Flowrate of VMS scrubbing liquor measured by FI 19308 (flow indicator) lower limit of 24 cubic metres/ hour flowrate Monitoring Point 3: Conductivity of VMS scrubbing liquor measured by CI 19309 (conductivity indicator) lower limit of 80 millisiemens/ centimetre conductivity VMS Performance Full year 2016 Huntsman has complied with the process conditions set in EOPO Licence 7494 (as amended 30- August 2016) for operation of the VMS. The licensed parameters are;

VMS - Scrubber liquor conductivity above 80 ms/cm CHART 1 VMS - Scrubber flow maintained above 24 m3/hr CHART 2 The charts show compliance to these requirements, for the 2016 calendar period, with the following clarifications; Brief Interruptions The charts show compliance to these requirements, with a few brief interruptions. Flow was lost due to pump trip tests, which total 80 seconds of flow below target (99.999% online). Conductivity was always above target there was a 2 second period of spurious signal. Note that scrubber takes several minutes to drain, therefore scrubber continues to remove oxide during these brief flow interruptions. Additional descriptions of each of these interruptions are included below. Also included (in appendices) are charts zoomed into the event times to confirm duration of each event.

CHART 1 DCS Trend for VMS Scrubber Liquor Flow CHART 2 DCS Trend for Liquor Conductivity

CHART 3 VMS Scrubber Liquor Flow Events There were 4 flow events that require scrutiny. Event 1 Pump trip tests 26-Jan-2016 Electric pump was tripped and diesel back-up pump started. Flow was re-established. Event 2 Pump trip test 5-Sep-2016. Testing conducted during planned total plant shutdown for preventative maintenance. Event 3 Pump trip and restart 20-Sep-2016 Duty pump was tripped and backup pump started automatically and reestablished flow in 10 seconds. Event 4 Pump trip and restart 1-Nov-2016 Duty pump was tripped and backup pump started. Flow was reestablished within in 10 seconds. Note that the test procedure has now been modified so that the duty pump is retained on-line while the automatic start of the backup pump is tested. This is indicated in the chart where the recirculation flow has increased to 70 m3/hr for short periods.

APPENDICES Additional records for events The charts below have zoomed into the event times to confirm duration of each event. Event 1 Pump trip tests 26-Jan-2016 Duty pump was restarted, total period of lost flow was 20 seconds (Note that scrubber takes several minutes to drain, therefore scrubber continues to remove oxide)

Event 2 Plant shutdown 5-Sep-2016. Pump shutdown as a result of planned total plant shutdown for preventative maintenance and routine trip & alarm testing. Restart of pump total of 40 seconds when flow was less than 24 m3/hr

Event 3 Plant trip tests 20-Sep-2016. Pump trip test and automatic start of back-up pump 10 seconds when flow was less than 24 m3/hr Note that scrubbing column takes several minutes to drain, therefore scrubber continues to remove oxide.

Event 4 Event 3 Plant trip tests 1 Nov-2016. Pump trip test and automatic start of back-up pump 10 seconds when flow was less than 24 m3/hr Note that scrubbing column takes several minutes to drain, therefore scrubber continues to remove oxide.