IS 14885:2001 specifies requirements for polyethylene (PE) pipes used for the supply of gaseous fuels, focusing on material quality, dimensions, mechanical properties, and performance under pressure and environmental conditions. It applies to manufacturers, suppliers, and engineers involved in the production, testing, and installation of PE pipes for gas distribution systems, ensuring safety, reliability, and compliance with national standards.
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168Clauses Indexed
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2001Edition
Plastic Piping SystemCategory
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Overview
What This Standard Covers
IS 14885:2001 specifies requirements for polyethylene (PE) pipes used for the supply of gaseous fuels, focusing on material quality, dimensions, mechanical properties, and performance under pressure and environmental conditions. It applies to manufacturers, suppliers, and engineers involved in the production, testing, and installation of PE pipes for gas distribution systems, ensuring safety, reliability, and compliance with national standards.
Audience
Who Uses This Standard
Pipeline Engineers
Gas Distribution System Designers
PE Pipe Manufacturers
Quality Control Inspectors
Material Suppliers
Construction Contractors
Regulatory Compliance Officers
Contents
Key Topics Covered
✓PE compound quality and classification
✓Dimensional requirements including outside diameter and wall thickness
✓Standard dimension ratio (SDR) and ovality limits
✓Hydrostatic pressure resistance testing at elevated temperatures
✓Long-term hydrostatic strength and creep rupture tests
✓Thermal stability and oxidation induction time (OIT)
✓Pigment dispersion and UV stabilizer limits
✓Mechanical tensile properties and elongation requirements
✓Marking, identification, and traceability of pipes
✓Sampling procedures and acceptance criteria
✓Squeeze-off test for maintenance operations
✓Visual and dimensional inspection protocols
✓Performance requirements under gas constituents exposure
✓Test piece preparation and testing apparatus specifications
Structure
Table of Contents
1Scope▼
IS 14885: Scope - Key Specifications & Tables
Scope Summary:
Covers dimensions, tolerances, performance, and sampling for polyethylene pipes.
1. Length of Pipe (Clause 6.4)
Length of straight pipes/coils as agreed between manufacturer & purchaser.
Ends: Cleanly cut, square to axis within tolerances (see Table 6).
Plus tolerance depends on nominal wall thickness (en):
Nominal Wall Thickness (en) mm
Plus Tolerance (mm)
2.0 to 3.0
0.4
3.0 to 4.0
0.5
...
...
29.0 to 30.0
3.1
(Refer to full Table 5 for detailed values)
3. Length and End Tolerances
Length: As agreed between manufacturer and purchaser (Clause 6.4).
Ends must be square within tolerance (Table 6):
Outside Diameter (mm)
Max Out of Square (mm)
16 to < 90
2
≥ 90 to < 140
3
≥ 140 to < 200
4
≥ 200 to < 315
5
≥ 315
7
Summary Diagram: Ovality vs Diameter for Straight Pipes
graph LR
A[Diameter ≤ 75 mm] -->|Ovality =
7Pipe Ends and Length Tolerances▼
IS 14885: Pipe Ends and Length Tolerances Key Points
1. Length of Pipe (Clause 6.4)
Length is as agreed between manufacturer and purchaser.
Ends must be cleanly cut, square to the axis, with tolerances per Table 6.
2. Out of Square Tolerance of Pipe Ends (Table 6)
Pipe Outside Diameter (mm)
Max Out of Square per End (mm)
16 to < 90
2
≥ 90 to < 140
3
≥ 140 to < 200
4
≥ 200 to < 315
5
≥ 315
7
3. Wall Thickness Tolerances (Table 5)
Plus tolerance varies with nominal wall thickness (en).
Example: For 5.0–6.0 mm thickness, tolerance = +0.7 mm.
4. Ovality Limits (Clause 6.1, Table 3)
Straight pipes ≤ 75 mm: Max ovality = 1 + 0.008 × d (d = outside diameter)
Straight pipes > 75 to ≤ 250 mm: Max ovality = 0.02 × d
Straight pipes > 250 mm: Max ovality = 0.035 × d
Coiled pipes ≤ 180 mm:
SDR 11: 0.06 × d
SDR 17.6: 0.15 × d
Summary Diagram: Pipe End Tolerances
flowchart TD
A[Pipe Ends] --> B[Cleanly Cut & Square]
B --> C{Diameter Range}
C -->|16 to <90 mm| D[Max Out of Square: 2 mm]
C -->|≥90 to <140 mm| E[Max Out of Square: 3 mm]
C -->|≥140 to <200 mm| F[Max Out of Square: 4 mm]
C -->|≥200 to <315 mm| G[Max Out of Square: 5 mm]
C -->|≥315 mm| H[Max Out of Square: 7 mm]
8Performance Requirements▼
IS 14885: Performance Requirements Summary
1. Dimensional Tolerances
Wall Thickness Tolerance (Table 5):
Varies with nominal wall thickness (en). For example:
Nominal Thickness (mm)
Plus Tolerance (mm)
2.0 - 3.0
0.4
10.0 - 11.0
1.2
29.0 - 30.0
3.1
Out of Square Ends Tolerance (Table 6):
Depends on pipe outside diameter:
Outside Diameter (mm)
Max Out of Square (mm)
16 to < 90
2
≥ 90 to < 140
3
≥ 315
7
2. Surface & Length Requirements (Clause 6.4)
Pipes must have smooth, clean internal surfaces free from defects affecting performance.
Length of pipes/coils as per agreement.
3. Acceptance Tests (Table 9)
Test Description
Clause
Sample Size Ref.
Dimensional checks
6.1, 6.2, 9.2.3
Table 10
Visual appearance
7, 9.2.3
Table 10
Hydrostatic pressure resistance (80℃, 165h)
8.1
Table 11
Reversion test
8.2
Table 11
Density, MFR, Pigment dispersion, Thermal stability (OIT), Tensile test
8.3-8.5, 5.4
Table 11
Key Formula for Hydrostatic Pressure Resistance:
[
\sigma = \frac{P \times d}{2 \times t}
]
( \sigma ) = hoop stress
( P ) = internal pressure
( d ) = pipe outside diameter
( t ) = wall
9Acceptance Tests▼
IS 14885: Acceptance Tests (Clause 9.2)
1. Types of Acceptance Tests (Table 9.2.1):
Test Description
Ref Clause/Table
Test Method
Hydrostatic pressure resistance at 80°C for 1000 h
8.1 Table 7
Annex A
Hydrostatic pressure resistance at 20°C for ≥100 h
8.1 Table 7
Annex A
Resistance to weathering
8.8
Annex F
Squeeze-off test
8.9
Annex G
Volatile matter content
8.6
Annex H
2. Acceptance Tests for Lot (Table 9):
Test Description
Requirement Clause
Sample Size (Table 10 or 11)
Dimensional checks
6.1, 6.2, 9.2.3
Table 10
Visual appearance
7, 9.2.3
Table 10
Marking information
10
Table 10
Hydrostatic pressure resistance @ 80°C for 165 h (plain pipes)
8.1
Table 11
Reversion test
8.2
Table 11
Density
8.3
Table 11
MFR (Melt Flow Rate)
8.4
Table 11
Pigment dispersion
5.4
Table 11
Thermal stability (OIT)
8.5
Table 11
Tensile test
5.4
Table 11
Hydrostatic pressure resistance @ 80°C for 165 h (Notched pipes ≥ 63 mm)
8.1
Annex A & B
3. Sampling Size for Visual & Dimensional Checks (Table 10):
No. of Pipes in Lot
Sample Size (1st)
Acceptance No.
Rejection No.
Up to
10Marking and Identification▼
IS 14885: Marking and Identification Key Points
Marking Method (Clause 10.1 & 10.2):
Marking must be permanent, legible, and impressed ≤ 0.2 mm depth.
Should not cause cracks or failures.
Must remain legible through storage, weathering, processing, and installation.
Marking Location (Clause 10.3):
Pipes ≤ 32 mm nominal size: single marking strip.
Pipes > 32 mm nominal size: two marking strips on opposite sides.
Marking Content (Clause 6.2 references):
Visual appearance
Marking information (manufacturer, size, standard, etc.)
Hydrostatic pressure resistance at 80°C for 165 h (plain and notched pipes ≥ 63 mm)
Pigment dispersion
Thermal stability (Oxidative Induction Time, OIT)
Summary Table: Marking Requirements
Pipe Size (Nominal)
Marking Strips
Marking Depth
Key Info Included
≤ 32 mm
1
≤ 0.2 mm
Manufacturer, size, pressure rating
> 32 mm
2 (opposite)
≤ 0.2 mm
As above + hydrostatic resistance
Important Notes:
Marking depth ≤ 0.2 mm prevents structural weakening.
Hydrostatic resistance at 80°C for 165 h confirms pipe durability.
Marking must withstand environmental and handling stresses.
flowchart LR
A[Pipe Size ≤ 32 mm] --> B[Single Marking Strip]
A2[Pipe Size > 32 mm] --> B2[Two Marking Strips (Opposite Sides)]
B & B2 --> C[Marking Depth ≤ 0.2 mm]
C --> D[Include Manufacturer, Size, Standard, Pressure Rating]
D --> E[Marking Legibility Maintained During Life]
This ensures pipe traceability and quality throughout service life.
Annex AHydrostatic Pressure Creep Rupture Test Method▼
Hydrostatic Pressure Creep Rupture Test (IS 14885)
Free length = 10 × outside diameter (min 250 mm, max 750 mm)
Summary Table for Notch Depth Calculation
Parameter
Symbol
Unit
Description
Mean pipe outside diameter
(d_m)
Annex DDetermination of Oxidation Induction Time▼
IS 14885 - Determination of Oxidation Induction Time (OIT)
Key Specifications (Clause 8.5 & Annex D)
Minimum OIT: ≥ 20 minutes at 200 ± 0.1°C.
Sample: Core drill samples from pipe wall; test pieces ~15 ± 0.5 mg discs from inner, outer, and mid-wall.
Pans: Open aluminium pans sized to hold test pieces.
Test Procedure Summary
Gas flow: Nitrogen at 50 ml/min ±10% initially.
Heating: Ramp at 20°C/min to 200°C ± 0.1°C; hold isothermally.
Switch gas: After 5 min nitrogen, switch to oxygen at 50 ml/min ±10%.
Record thermogram: Plot temperature differential vs. time.
OIT determination: Time from oxygen introduction to intersection of baseline and tangent at max exotherm slope.
Interpretation (D-4)
OIT = time (min) from oxygen start to oxidation exotherm onset.
Average at least 5 measurements for thermal stability.
Test Report Must Include (D-5)
Test piece ID
Reference to IS 14885 method
Individual OIT results (min)
Test date
Diagram: OIT Determination Thermogram Concept
graph LR
A[Nitrogen Flow] --> B[Heat to 200°C]
B --> C[Hold Isothermal]
C --> D[Switch to Oxygen]
D --> E[Oxidation Exotherm]
E --> F[Draw Tangent at Max Slope]
E --> G[Extend Baseline]
F & G --> H[OIT = Intersection Time]
Additional Notes
Anti-oxidant content ≤ 0.3% by mass (IS 2530).
Follow instrument manufacturer instructions except where IS 14885 specifies otherwise.
This method ensures reliable assessment of polymer thermal stability via OIT.
Annex GSqueeze-Off Test Method▼
IS 14885: Squeeze-Off Test Method (Clause 8.9 & Annex G)
Key Specifications:
Pipe Size: Up to 400 mm diameter.
Conditioning: Pipe conditioned at 0°C (+0, -5°C) for minimum 10 hours.
Squeeze-Off: Within 10 min after conditioning, the pipe center is squeezed-off to the smaller separation value specified by the manufacturer or code.
Squeeze-Off Duration: Maintain squeeze-off for at least 60 minutes.
Test Temperature: Specimen tested at 80°C.
Stress Levels:
PE-80: 4.6 MPa
PE-100: 5.5 MPa
Test Duration: Must withstand stress for minimum 165 hours.
Mandrel Size:
As per ASTM F 1041-92 (mandrel size corresponds to pipe diameter and squeeze-off level).
Minimum Squeeze-Off:
30% minimum squeeze-off (i.e., pipe diameter reduced by at least 30%).
Post-Test Requirements (Clause 8.8):
Hydrostatic strength at 80°C for 165 h.
Minimum elongation at break: 350%.
Oxidative Induction Time (OIT) after weathering at 200°C.
Summary Table:
Parameter
PE-80
PE-100
Conditioning Temp
0°C (+0, -5°C)
0°C (+0, -5°C)
Conditioning Duration
10 h
10 h
Squeeze-Off Duration
60 min
60 min
Test Temp
80°C
80°C
Stress Applied
4.6 MPa
5.5 MPa
Test Duration
165 h
165 h
Minimum Squeeze-Off
30% pipe diameter reduction
Process Flow (Mermaid Diagram):
flowchart TD
A[Condition pipe at 0°C for 10 h] --> B[Squeeze-off pipe center to ≤ specified separation]
B --> C[Maintain squeeze-off for 60 min]
C -->
Annex JTesting Machines and Test Pieces▼
IS 14885: Testing Machines & Test Pieces - Key Points
1. Measuring Instruments (Clause 3.2)
Use a micrometer accurate to 0.01 mm for measuring width and thickness of test pieces.
2. Test Pieces (Clause J-4 & Fig. 6)
Type 1/2 Test Piece: For tensile properties of smaller diameter pipes.
Key dimensions:
H (initial clamp distance): 60 ± 5 mm
Reference lines: A (length), B (width ends), C (calibrated length), D (calibrated width), E (radius), G (distance between lines).
3. Selection of Test Pieces (Table 12, Clause 4.2.2)
Wall Thickness (e) mm
Test Piece Type
Thickness of Test Piece (F)
Remarks
e < 5
1/2 or 2
e
Non-machined
5 < e ≤ 10
1
e
Non-machined
e > 10
1
10
Machined (smooth surface, no heating)
Machined pieces: Thickness reduced to 10 mm; inside surface machined for first series.