2 4ueda PDF
2 4ueda PDF
2 4ueda PDF
Schedule
Conclusions
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1.Risk assessment process chart of chiller SWG
The working group , which consists of professional chiller engineers, in Japan Refrigeration
and Air Conditioning Industry Assosication (JRAIA) started in 2011.
Risk assessments(RAs) were executed until last year and the guideline(GL) draft was
created at the end of 2014, which is now being deliberated to be issued as the guideline
during this fiscal year.
JRA-GL◆
Kobe symposium◆ Kobe symposium◆ Final report◆
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2. Risk assessment and legal system
4.リスクアセスメントの構成概要(1)
Industrial Safety
and Health Law
【Order for Enforcement 】
A workplace employing a certain number of workers shall
appoint a General Safety and Health Manager.
【Enforcement Regulations】
The Building The General Safety and Health Manager shall perform risk
assessments.
Standards Act EN1127-1(2011)
JRA Explosive atmospheres –
Explosion prevention and protection
High Pressure Gas -GL15
Safety Act
Guideline of
design IEC60079s(2011)
construction for
Explosive atmospheres – Equipment
Refrigeration Safety Regulations ensuring safety
Article 7.14 Electrical Equipment refers to against refrigerant ;General requirement
leakage form
explosion preventive performance ・・ chillers using JIS60079s
mildly-flammable Electric Machinery and Instruments Used in Explosive Atmospheres
refrigerants General Requirements is the 2007 version of IEC.
>Outdoor natural ventilation=Zone2
KHK0302-3(2012) >forced ventilation with preliminary and warning devices.
Standards of Refrigeration and Air-Conditioning +normally, explosive atmospheres are not formed.
Equipment Facilities〔Fasilities with Flammable Gases =Zone2NE(not dangerous)
(including mildly-flammable Gases)〕
ISO5149
Refrigeration system and heat pumps – safety
and environmental requirements
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3.Target products
Ebara
Mitsubishi Refrigeration
Mayekawa Kobe Steel Heavy Equipment
Industries And Systems Mitsubishi Electric Toshiba-Carrier Hitachi Appliacnes
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4
4. Acceptable probability of harm
5
Probable 10-4 10-2 (1.0X10-2) once a year per 100 units
4
Probable 10-5 10-3 (1.1X10-3) 134 times a year
3
Remote 10-6 10-4 (1.1X10-4) 14 times a yea
2
1 Improbable 10-7 10-5 (7.5X10-6) once or twice a year
0
-7 once or twice
Incredible 10-8 10-6 (7.5x10 ) every ten years
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5. Definition of life stages
Ratio of
Life Number Number of
Target Work content LS ratio
Stage sale
AC WC
Transpotation and storage in
Logistics Supplier warehouse Total 9,687 0.0517
Carrying in・Installation・Storage・
Installation Trial operation 7 3 9,687 0.0517
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6. FTA and calculation method of probability (1)
Basic FTA was configured to align the probability of refrigerant leakage and probability of
existence of ignition sources in 6 Life Stages (LS)(Figure.5).
Probability of ignition during life stages
Presence of an Presence of
Important as
iginiton source(#1) flammable space Probability of measures
occurrence
Calculated by
Probability of existence of
ignition sources Probability of Lack of No-operation of the detector
× refrigerant leak (#2) ventilation and the shut-off device
Probability of leakge
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7. FTA and calculation method of probability (2)
In order to detect all the probable ignition sources, FTA common to all life stages was configured for
calculating the probability of the existence of ignition sources and prbability of leakage.
Probability of the existence of an ignition source (common to each life stage)
Control
Butt throw-in panel
boiler Direct flame
・ power ・
・ Start-up
equipment ・
・ panel ・
Internal equipment
wiring wiring
electrical Electrical
component component
・ ・
・ ・
・ ・
Table 8 Frequency of leakage occurrence for each leakage rate from fiscal 2004 to 2011.
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9. Machine room model (Image)
Overview of the chiller machine room
(1) Probable Ignition sources are a boiler with a burner (only the surface temperature should be considered) , a hot and
chilled water generator, starter panels, power panels, and electrical components (breakers and solenoid switches) in the
operation panels of chillers and pumps
(2) Building Standard Act indicates the values of (oxygen consumption, heat removal, oxygen concentration)corresponding
to ventilation and actual circumstances.
(3)Exhaust from the burning appliances such as the boiler and the absorption chiller by direct boiling is discharged outside through
independent duct.
(4)Exhaust air is not discharged to other rooms and does not affect outdoor air exhaust and air intake into other buildings.
(5)Ventilation is 2 air-changes /h ×2 lines , totaling 4 air-changes /h(ISO5149)
Smoking Match No No
supplies Oil lighter No No
Human Static electricity emitted from a No Minimum ignition energy or less No
body human body
Open Smoking Match Yes Ignition=open fire 4.72x10-9
flame supplies
Oil lighter Yes Open fire once ignited 1.18x10-6
Electric lighter No Lighter not ignited
Burning Electric radiant heater Yes Prohibited to use 3.30x10-6
appliance
Electric fan heater No Prohibited to use No
Gas water heater Yes Prohibited to use No
Gas boiler(burner ) No No timing of ignition No
Ventilation duct, boiler surface No 140℃ or below No
Gas cooking appliance Yes Prohibited to use No
Work tool Burner for brazing No High in gas velocity No
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11. Machine room model(installation layout)
A room with the height of 5m and the floor area with the horizontal and longitudinal length ratio of 1:2 was assumed, in
which a chiller was installed on one half of the floor area and auxiliaries were installed on the other half.
As the maintenance space, the clearance of at least 1.2m in front of the control panel and 1.0m from other surface was
assumed.
The leakage point was assumed to be located at the height of 0.15m from the floor and the shape of the leakage point was
cylindrical nozzle of 0.10m length.
Suction port Exhaust port
1.245 m 1.245 m
0.88 m
The target 1.01 m
machine
0.88 m 5.0 m (Side of Control panel)
0.88 m 1.28 m
3.3 m
The target 1.01 m
machine 1.21 m
1.28 m
6.6 m
3.3m
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12. CFD Analysis result of machine room
Table 12 Unsteady state analysis result(machine room)
Figure 12.1 Analysis result of concentration and time dependent volume Figure 12.2 Analysis result of concentration and time dependent volume
(R1234ze(E)wet, air change:0 times, rapid leak) ( R1234ze(E)wet, air changes:4 times, rapid leak)
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13. Air-cooled Heat Pump Model for CFD
12.空冷HPモデルの特定
An air-cooled HP installed outdoors and lacking walls on all four sides has low chance of forming a flammable space compared to water-
cooled chiller installed in the machine room. Based on the soundproofing installation procedure described by the manufacturer, the analysis
model including four walls, two plain walls and two with an aperture of 25%, where flammable space is most possibly formed, are assumed.
The following two refrigerant leakage points were assumed. (Figure.13.2)
Leakage point ①Leakage from the air heat exchanger of the outdoor unit
・In the center of the front surface of the unit and at the height of 0.15m from the heat exchanger on the floor.
・Slow leak:I.D of 1mm Rapid leak:I. D. of 4mm Burst leak:I.D. Of 8mm(The diameter of the nozzle shall be the length at which the
refrigerant leaks at the velocity of sound)・Leakage direction:horizontal
Leakage point ②Leakage from the unit inside the bottom panel of the outdoor unit
・The apertures of 2m×10mm in the middle of the both side bottom panels with the longitudinal length of 3m were assumed.
・The bottom panel other than those regions were assumed hermetic. ・Leakage direction:horizontal
Figure 13.1 Air-cooled HP analysis model (wall aperture) Figure13.2 Air-cooled HP analysis model(leakage point)
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14. CFD Analysis result of Air cooled HP
In case of leakage from air heat exchanger, the flammable space is very small and negligible.
Meanwhile, in case of leakage from the aperture of the bottom panel , the refrigerant accumulates in
the lower region of the unit forming flammable space.
Table 14 Unsteady state analysis result(Wind velocity 0m/s)
Unit horse Leakage velocity Time dependent
Leakage point Refrigerant Case of leak
power [Hp] [kg/h] volume [m3min]
Air heat R32 Rapid leak 10 0.0002
exchanger R1234ze(E) Rapid leak 7.3 0.0003
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15. Probability of accidental fire
Integrated value of the probability of ignition is calculated both for with and without ventilation.
With ventilation, the highest probability of ignition is 10-12 . Therefore, it was evaluated as
”Incredible”.
Risk assessment result Probability of ignition(times/year・units)
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16. Measures and guidelne
1. Installation of mechanical ventialtion
:2 air-changes/h×2 lines
with backup to guarantee ventilation effectiveness .
Air intake from the above and exhaust from the
bottom.
Controllable from outside the machine room
2. Installation of refrigerant leakage detection and
warning device
Operation with independent power source
such as UPS, installed in the place where
refrigerant could accumulate.
4. Inspection
Compulsory inspections of mechanical ventilation and refrigerant leakage detector at
appropriate frequency.
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17. Conclusion
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Thank you for your attention.
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