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Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
USATAIWANJAPANCHINA
Fire Safety ComplianceWhy Are My CO2 Systems Not S2 Compliant?
For2010 SESHA Hill Country
By Matt Wyman, Managing Director
KFPI Inc.September 28, 2010
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
USATAIWANJAPANCHINA
Overview
1. SEMI S22. Fire Safety Requirements
1. SEMI S2 Chapter 14
3. Non Compliance Findings4. Cause 5. Solution
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
USATAIWANJAPANCHINA
KFPI Services Equipment Fire Protection Systems
Carbon Dioxide (CO2) Fine Water Spray (FWS) Aspirating Smoke Detection (ASD) Flame Detection (Multi IR)
Consulting Risk Engineering Analysis & Consulting Equipment Safety Compliance Compliance Audits & Testing Training
IR Thermography Thermal Scans Reports
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
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KFPI Leadership SEMI© Standards Fire Protection Task Force
Chairman (Past & Present) NFPA 318 Clean Room Fire Protection Committee
Chairman (Past) Factory Mutual (FM Global) Semiconductor Specialist
(Past) Factory Mutual Research Board (FMRC)
Advisory Board Member (Past) Expert Witness on International Fire Loss Litigations Published Numerous Papers in Industry Magazines Presented Numerous Papers in Industry Venues Global Training Seminars
Fabricators, Insurance, & 3rd Party Consultants
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
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SEMI S2 Compliance Environmental, Health, & Safety Guideline for
Semiconductor Manufacturing Equipment Required by Fabricators Worldwide Categories Include:
Hazard Warning Labels Safety Interlock Systems Emergency Shutdown Electrical Design Fire Protection Heated Chemical Baths Ergonomics and Human Factors Hazardous Energy Isolation Mechanical Design
Seismic Protection Automated Material Handlers Environmental Considerations Exhaust Ventilation Chemicals Ionizing Radiation Non-Ionizing Radiation and Fields Lasers Sound Pressure Level
Fire Protection
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Safety Labels
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Chemical Safety
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Hazardous Energy
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Radiation
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Laser
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Emergency Shutdown
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Fire Codes International Fire Code (IFC)
Combustibles or Flammables >4ft. Wide Sprinkler Head Inside or Gaseous Fire Suppression
FM DS 7-7 “Semiconductor Fabrication Facilities” Equipment Protection Design Criteria CO2 & FWS 13kW Fire Detection
NFPA 12 “Carbon Dioxide” (FM4-11N) NFPA 750 “Fine Water Spray” NFPA 318 “Protection of Semiconductor Fabrication Facilities” SEMI S14 “Safety Guidelines for Fire Risk Assessment &
Mitigation for Semiconductor Manufacturing Equipment” SEMI S2 “Environmental, Health, & Safety Guideline for
Semiconductor Manufacturing Equipment” Chapter 14 “Fire Protection”
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
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S2 Compliance Section 14.4.4 Fire Detection, Alarm , & Controls 14.4.4.1&2 All detectors, alarms, and controls be accepted and listed by an
accredited laboratory (example UL or FM) and installed in accordance with the terms of that acceptance and appropriate national or international standards (example NFPA 72).
14.4.4.3 Capable of interfacing with facility’s alarm system 14.4.4.4 Activate alarms audibly and visually at equipment
Note 58 Should be identifiable & distinguishable from other alarms 14.4.4.5 Manual activation should be considered 14.4.4.6 A supervisory/trouble condition should notify operator, allow
completion of existing processing, but prevent additional processing until condition is cleared.
14.4.4.7&8 Capable of operation at all times with 24hr backup batteries 14.4.4.11 Shut down the equipment upon alarm condition (EMO) 14.4.4.12 Capable of being certified by licensed parties
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
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S2 Compliance Section 14.4.5 Fire Suppression 14.4.5.1 The fire suppression system, which includes nozzles, actuators, and their
associated controls, should be certified by an accredited testing laboratory (e.g., UL or FM) and suitable for the application and for the environment in which it to be used.
14.4.5.2&3 The fire suppression agent and delivery system should be designed and installed in accordance with the appropriate international or national standard (e.g., NFPA 12).
14.4.5.5 Activate alarms audibly and visually at equipment Note 64 Should be identifiable & distinguishable from other alarms
14.4.5.10 Allowance can be made to disable system when in maintenance mode if supervised.
14.4.5.11 Capable of operation at all times with 24hr backup batteries 14.4.5.12 Capable of interfacing with facility’s alarm system 14.4.5.13 Shut down the equipment upon alarm condition (EMO) 14.4.5.14 Manual activation should be provided 14.4.5.15 Should be discharge tested on represented sample of equipment 14.4.5.16 Control access to the suppression agent source. 14.4.5.17 Capable of being certified by licensed parties 15.4.5.19 Piping should be designed, installed, and tested to ensure it is capable of
withstanding discharge pressures.
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CO2 Hazard Design Total Flood (TF) Design
Fully Enclosed Compartments Criteria = 50% CO2 Concentration Time Limit = 60 Seconds Compensate for
Exhaust Ventilation Uncloseable Openings
Local Application (LA) Design Open Compartments
Example = Working Surface Criteria = Minimum Flow Rate Time Limit = Minimum 30 Second Compensate for
Missing Walls Not for Exhaust
Combination Design Both TF & LA
0
10
20
30
40
50
60
0 15 30 45 60
MinimumNot ProtectedProtected
CO2 Concentration Levels
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
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Non-Compliance Findings
All found on existing CO2 Systems 3rd Party Reviews Site Audits Design Reviews Incident Investigations
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Inadequate Designs
Total Flood (TF) Hazard Exhaust Compensation
Not Included (or Damper) Exhaust Not Distributed
Uncloseable Opening Leakage Wrong Flooding Factors
Local Application (LA) Hazard Assumed Volume Calculations % Perimeter Closed 60-sec Discharge Duration
Copyright © 2010 KFPI Inc., All Rights Reserved SESHA 2010
Assumed Volume (LA)
LocalApplication
Headcase Headcase
Working Surface
Plenum
Front View
Pumps/Heaters
ProcessTank
Side View
TotalFlood
TotalFlood
None
ActualVolume
AssumedVolume
4.0ft.Minimum
Height
Add2.0ft.OpenSides
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Assumed Volume (LA)
4.0ft.Minimum
Height
AssumedVolume
ActualVolume
Example:IPA DRYERLA Design
Add 2.0ft.To Each Side
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CO2 Nozzles LA Nozzles
All have “cone” to absorb discharge pressure
Reflected discharge from orifice Less exit velocity (same flow rate) Nozzle absorbs most 600psi
discharge pressure
TF Nozzles “V” Nozzle is “Vent” nozzle (TF) Straight discharge from orifice Full effects of ~600psi discharge
pressure on tool (especially baths) Much higher velocity
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TF Nozzles Used in LA Hazards Ansul & Hatsuta
FM Approved LA Nozzles for Wet Bench
Stainless Steel (SS) & Halar Coated Kidde & Others (Fenwal, Fike)
No FM Approval for Wet Bench No SS or Halar Coated Models Painted Steel/Brass/Chrome Not
Compatible with Wet Processing
LA Nozzles Installed Heights Above Coverage Chart All LA Nozzles Have Coverage Chart
Nozzle Issues
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Hydraulic Calculations UL/FM Approved Calc Software
Based Upon Liquid Discharge Time Increase Capacity ≠ Increase Concentration
More Agent ≠ Adequate Design Extends Discharge Duration
Inadequate Hydraulic Calculations Supply ≠ Demand Discharge Duration > Demand Manufacturer Specific CO2 Distribution ≠ Installation
See Example 0
10
20
30
40
50
60
0 15 30 45 60
MinimumNot ProtectedProtected
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Hydraulic Calcs
Sample Hydraulic Calc Report (Pipe & Tubing)
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Hydraulic CalculationsWET
BENCHHazard 1
LAHazard 2
TFHazard 3
TFCO2
Supply
CO2 Demand 64.8 lbs 84.2 lbs 13.2 lbs. 200 lbs.
# Nozzles 4 2 1 2 cylinders
H1 = 20.5lbs/42.6sec x 30sec = 14.44 x 4 nozzles= 57.8 lbs
H2 = 51.0lbs/42.7sec x 30sec= 35.8 x 2 nozzles= 71.6 lbs
H3 = 16lbs/42.6sec x 30sec = 11.2 lbs x 1 nozzle= 11.2 lbs
This hydraulic calc is inadequate End of Report is Nozzle Summary
Must Verify Supply = Demand
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CO2 Distribution High Pressure CO2 Cylinders
Stored Pressure = 750psi Nozzle Pressure = ~350psi – 650psi
Must have internal pressure rating of 3,000 psi Must have internal burst pressure rating of 5,000 psi SS Piping is Allowed by Fire Code (NFPA 12 – Section 4.7)
Pipe ≤ ¾ in. = Schedule 40 Pipe ≥ 1 in. = Schedule 80 with Extra Heavy Fittings
Recommend SS Tubing (316) with SS Compression Fittings Minimum Wall Thickness Cleanliness & Contamination
Questions? How Do You Verify Integrity? CO2 Discharge?
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CO2 Distribution Issues Compression Fittings Not
Installed Correctly Compression Fittings
Installed on Pipe vs. Tube ¾” Fitting on ½” Pipe
Calculated with Pipe installed with Tubing ½” Pipe ID > ½” Tube ID ½” Pipe ID ≠ 5/8” Tube ID Friction Coefficient Not Equal
1.0”+ Pipe Installed with Schedule 40 Fittings
Improper Tubing Thickness
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Exhaust Dampers
Exhaust Damper Not Allowed NFPA 318 Section 5.3.5 SEMI S2 Exhaust/Chemical Safety
Solvent Fumes (LEL) Corrosive Fumes
FM DS 7-7 Section 2.5.15.1.2
Exhaust Ventilation Reduces Smoke Damage Exhaust Volume >> Compartment Volume
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Flame (Optical) Detectors
Semiconductor Industry 4 Flame Detectors FM Approved for Use on Wet
Benches Sierra DCR1 (UV/IR) Det-Tronics PM-5MPX (IR) Fire Sentry FS7 (IR) Hatsuta SX-7000 (IR)
Field Of View (FOV) Coverage Affected by Physical Obstructions Coverage Affected by Detector Range
120º FOV
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Flame Detector Issues
Compliance Issues: FOV Obstructed Spacing > 13kW
8” PP Fire 4” IPA Fire
Chemical Compatibility UV ≠ HF Quartz Window
Match Detector with Fuel
ObstructedView
DetectionArea
Detector
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Lockout Valves Lockout Valves (NFPA 12 2005)
Required except where personnel can’t enter space (4.3.3.6) Where CO2 can migrate to expose personnel (4.3.3.6.1) System should “Lockout” during maintenance or testing
(4.3.3.6.3) “Lockout” Valve must be supervised
Lockout Valve Typically Not Required If a Lockout Valve is Installed then….
Pressure Switch installed between Supply and Lockout Valves (4.5.4.11)
A Pressure Relief Valve is Required (4.7.2.4) Operate 2400-3000psi
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Disable/By-Pass Switch (Required but Not Installed) Electrically operated systems should have service disconnect switch
(NFPA 12 – Section 4.3.3.7) Switch must be supervised (by panel)
Electrical Lockout of Discharge Tool Maintenance or System Testing/Inspection
Key Switch – “Lockout”Key Switch – “Normal”
Disable Switch
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Personnel Device Issues Horn/Strobe
Not ADA/NFPA Mounting Heights 80-96” AFF
Adequate Notification for Personnel? All 4 Sides of Tool? Bay/Chase or Fab/Subfab
Manual Release Not ADA/NFPA Mounting Heights
48-52” AFF Mounted Above Fire Hazard
Adequate Travel Distance? Bay/Chase or Fab/Subfab
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Wiring Installation Issues
All Fire Alarm Inputs & Outputs are Supervised EOL Resistors @ Panel (Not EOL) Fault Relays Not Supervised
Flame Detectors Aspirating Smoke Detectors
Cables Not Protected NEC / NFPA
Wire Gauge Too Small NEC / NFPA
EOL Resistor
Panel Input
EOL Resistor
Alarm
Fault
Detector
Panel Input
Device
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Inadequate Battery Calcs Result is < 24hr. Standby & 5min Alarm
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Chemical Compatibility Issues CO2 Components Must Be Chemically Compatible
Nozzles & Detectors
Combustible Plastic Benches Corrosives
Single Wafer Processing Tools Solvents & Corrosives
Nozzles, Tubing, & Fittings Must be Coated & Sealed
Detectors Must be Compatible with Corrosives HF & Quartz are Not Compatible
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Safety Label Issues No CO2 Safety Labels Labels must meet ANSI Z535
Orange “Warning” Color “Warning” Triangle Symbol Aspiration Symbol
Outside Protected Space At Manual Activation SEMI S1 Compliant
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Kidde Issues Kidde “V” (Vent or Velocity) Nozzle is TF Nozzle
Kidde Only Manufactured “V” Nozzle in Brass June 2005 Kidde Released Stainless Steel “V” Nozzle
FM ApprovalGuide
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Imitation (Copy) “V” Nozzles
Result was Imitation Kidde “V” Nozzles Supplied to Industry prior to 2005.
These same Imitation Nozzles Are Still Being Used Today
No Threads
USA VERSION
No Strainer
Installed Backwards
TAIWAN VERSIONREAL KIDDE
Result is S2 Non-Compliance Nozzle CO2 System Tool
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Cause Why Has This Happened? Fire Protection has NOT Been Reviewed as Part of SEMI S2
Report. Fire Protection has NOT Been Reviewed by Site Safety
Personnel (Product Safety). Majority of Equipment CO2 Systems are NOT Reviewed by Fire
Department or Insurance. 99% EHS Professionals Come from EHS, IH, Ergonmics, etc.
Background No Fire Protection Engineering or Fire Safety Background
Fire Protection is a Professional Engineering Discipline Must have 3rd Party Approval & Certification for Compliance
CO2 & FWS Specialized Fire Suppression Application Not Used by Majority of Fire Contractors
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Solution What is the Solution? Verify SEMI S2 Reports Include Fire Protection Verify SEMI S2 Reports are Completed by Qualified Personnel Require Copies of Fire Design Package Documentation
OEM, 3rd Party, Fire Contractor Have Safety Personnel to Review Design & Reports
Property Insurance Carrier Equipment Safety Personnel for Fire Safety Compliance
Verify Insurance Agent Qualified to Review CO2/FWS Systems Provide Training Corporate Level or at Site Level
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Questions Fire Protection Is Not Needed Often…………..
But When It Is…………It Has To Work!
It Also Must Be Reliable………..To Prevent Damage & Downtime!
Matt Wyman, Managing DirectorAdvanced Technologies DivisionSemiconductor, TFT-LCD, & PV
KFPI INC.Koetter Fire Protection International Inc.
USA – TAIWAN – JAPAN - CHINA(1) 972.333.4965 – [email protected]
www.kfpiinc.com