EXECUTIVE SUMMARY

A study (Protocol # IS210-TI-006) was carried out to compare the impact, if any, of EO concentration on product EO residual levels determined in accordance with ISO10993-7. Product samples were provided by a major medical device manufacturer for evaluation in the study. Samples of three device types were exposed two cycles with identical parameters with the only exception being one had a calculated EO concentration of 600mg/l and the other was 300mg/l.

Samples were retrieved immediately after the sterilizer primary aeration phase and stored appropriately in frozen conditions to prevent any further aeration while awaiting EO residual testing. The samples were extracted in H2O for 24 hours at 37°C and tested for EO residuals. One of the devices contained multiple materials so each material in this product was tested separately.

INTRODUCTION

The purpose of this study is to investigate the impact of EO concentration during the EO exposure phase of a sterilization cycle on the EO residuals remaining on the product on completion of the cycle.

REFERENCE DOCUMENTS
ISO11135:2014 Sterilization of health-care products — Ethylene oxide — Requirements for the development, validation and routine control of a sterilization process for medical devices
ISO10993-7:2008 Biological evaluation of medical devices – Part 7: Ethylene oxide sterilization residuals
IS210 -TI-006 Trial Cycle Instruction – Phase 1: EO Residuals by EO Concentration

 

MATERIALS & METHODS

Two EO cycles were performed as per Table 1, using the same dunnage load to minimize processing variables. The dunnage load included six pallets of bulk-packed disposable polypropylene syringes and two pallets of PVC tubing devices to fill an eight-pallet sterilization chamber. The load was allowed to aerate for 3 days at 30°C +/- 5°C between cycles to eliminate the carry-over of residues from one run to the next.

Samples of medical devices were provided by a leading device manufacturer for placement on each cycle and subsequent testing for residuals. The samples of each device were placed in triplicate in each cycle. They were placed in the same carton on top of pallet one of the dunnage load (PP syringes). The test samples comprise

  • Device 1: Suction device comprising of rigid PVC
  • Device 2: Auxiliary tubing comprising of soft PVC
  • Device 3: Enteral feeding set comprising of PVC tubing, polypropylene spike connector and PVC welded bag

On completion of primary aeration, the load was removed from the process and samples retrieved from the load. The samples were frozen to approximately -18°C within 30 mins of cycle completion to halt further aeration pending testing.

DISCLAIMER

Please note, this was a very limited study involving a select number of polymeric materials and a single EO process with varying EO concentrations. Further investigative work is required to arrive at a generic conclusion that may be applied to medical devices in general.

Table 1: CYCLE PARAMETERS @ 300 mg/l & 600 mg/l EO Concentration
STAGE PHASE PARAMETER SET POINT AT 300 mg/l SET POINT AT 600 mg/l
Pre-Conditioning Cell Temperature 50 °C 50 °C
Relative Humidity 60% 60%
Dwell Time 8 hours 8 hours
Cell to Chamber Transfer Time N/A N/A
Exposure Vacuum Evacuate to: 100 mbar 100 mbar
Time N/A N/A
Chamber Temperature Outside Initial Vacuum and EO Dwell 50 oC 50 oC
Leak Test Pressure Increment 0 mbar 0 mbar
Stabilization Time 1 min 1 min
Dwell Time 7 min 7 min
N2 Flush Pressure 600 mbar 600 mbar
Time N/A N/A
Re-evacuation Evacuate to: 100 mbar 100 mbar
Time N/A N/A
Conditioning Repeats 4 4
Steam Injection Pressure 140 mbar 140 mbar
Time N/A N/A
Dwell Time 12 min 12 min
Vacuum Evacuate to: 110 mbar 110 mbar
Time N/A N/A
EO Gas Injection Pressure 293 mbar 476 mbar
Time N/A N/A
Gas Supply Temperature N/A N/A
Chamber Temperature 50 °C 50 °C
EO Gas Dwell Chamber Temperature 50 °C 50 °C
 Dwell Time 180 min 180 min
1st Post-Exposure Vacuum Pressure 100 mbar 100 mbar
Time N/A N/A
Steam / Nitrogen Washes Repeats 10 10
Steam Injection Pressure 125 mbar 125 mbar
Time N/A N/A
Nitrogen Injection Pressure 200 mbar A 200 mbar A
Time N/A N/A
Vacuum Pressure 100 mbar A 100 mbar A
Time N/A N/A
Air Washes Repeats 2 2
Air Injection Pressure 600 mbar A 600 mbar A
Time N/A N/A
Vacuum Pressure 100 mbar A 100 mbar A
Time N/A N/A
Final Air Admission Pressure Atmospheric Atmospheric
Time N/A N/A
Chamber to Cell Transfer Time N/A N/A
Degassing Primary Cell Temperature 50 oC 50 oC
Time 8 hours 8 hours

 

Residuals testing was performed using cut up and immersion extraction into water at 37°C for 24 hours in accordance with ISO10993-7.

Device 1: Entire product

Device 2: A 30cm sample was taken from the middle of the tube for testing as a representative sample portion

Device 3a: A 30cm sample was taken from the middle of the tube for testing as a representative sample portion

Device 3b: The entire bag

Device 3c: The entire spike

Testing was performed using Gas Chromatography validated for testing of EO residuals in accordance with ISO10993-7. Detection was via an FID detector at 300°C. The concentration of EO and ethylene chlorohydrin (ECH) were calculated from the resultant data generated.

RESULTS: COMPARISON OF EO RESIDUAL OUTCOMES

The following tables summarize the results of the different levels of EO concentration on the product EO residual outcomes.

Device 1 – Rigid PVC Yankauer
Device 1 – Rigid PVC Yankauer
600mg/l cycle 300 mg/l cycle  
EO (ppm) EO (mg/device) EO (ppm) EO (mg/device) % Reduction  
358.81 3.62 123.72 1.25    
360.02 3.64 126.80 1.28
364.98 3.72 134.89 1.35
361.27 3.66 128.47 1.29 64%  

 

Device 2 – Soft PVC Auxiliary Tubing
Device 2 – Soft PVC Auxiliary Tubing
600mg/l cycle 300 mg/l cycle
Sample EO (ppm) EO (mg/device) EO (ppm) EO (mg/device) % Reduction
1 1555.01 30.98 632.77 12.67  
2 1379.84 26.87 636.09 12.67
3 1893.07 37.10 798.62 16.38
Average 1609.31 31.65 689.16 13.91 57%

 

Device 3a – PVC Bag
Device 3a – PVC Bag
600mg/l cycle 300 mg/l cycle  
EO (ppm) EO (mg/device) EO (ppm) EO (mg/device) % Reduction  
62.21 1.44 19.96 0.46    
61.53 1.38 19.95 0.46
48.69 1.11 18.72 0.43
57.48 1.31 19.54 0.45 66%  

 

Device 3b – PVC Tubing
Device 3b – PVC Tubing
600mg/l cycle 300 mg/l cycle  
EO (ppm) EO (mg/device) EO (ppm) EO (mg/device) % Reduction  
215.60 0.47 69.37 0.16    
78.88 0.18 40.12 0.09
82.81 0.18 51.15 0.12
125.76 0.28 53.55 0.12 57%  

 

Device 3c – PP Spike Connector
Device 3c – PP Spike Connector
600mg/l cycle 300 mg/l cycle  
EO (ppm) EO (mg/device) EO (ppm) EO (mg/device) % Reduction  
336.73 0.62 159.50 0.29    
332.78 0.61 138.25 0.25
300.99 0.55 144.63 0.26
323.50 0.59 147.46 0.27 54%  

 

DISCUSSION

From the results of this limited study, it can be seen that a 50% reduction in EO concentration resulted in an associated reduction in EO residual levels on the materials used in the products tested within the study. In the case of PVC, both rigid and soft grades, the resulting reduction in product residuals was greater than 50%.

It can be concluded from this study that reducing EO concentration in an EO cycle will result in lower residuals on product, which in turn could result in shorter aeration times to meet the limits set out in ISO10993-7: 2008

Authors:

Keith Beaumont, Validation Manager (BSc)
Brian McEvoy, Senior Director, Global Technologies (MBA, BSc)
Richard Cowman, Technical Director-Global EO, (BA, Dip. Applied Biology)

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