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IS 13488 - 2008
IRRIGATION
EQUIPMENT– EMITTING
PIPE SYSTEM
SUBMITTEDTO– JAGANS. MEHTASIR
SUBMITTEDBY – TUSHARRANJANSARKAR
COURSE– PGD-PPT3RD SEMESTER
ROLL NO. - 220106017
What is Emitting Pipe ?
Emitting Pipe play a key role in drip irrigation systems. Emitting pipes are manufactured from
virgin special grade polyethylene. Resistant to Ultra Violet (UV) radiation and other
environmental effects . Emitting Pipe passes through stringent quality tests confirming to Indian
and International Standards .The nominal diameter ranges from 12 mm to 25 mm.
Benefits of Drip Irrigation
Drip irrigation involves placing tubing with emitters on the ground along side the plants. The
emitters slowly drip water into the soil at the root zone. Because moisture levels are kept at
an optimal range, plant productivity and quality improve. In addition, drip irrigation:
•Prevents disease by minimizing water contact with the leaves, stems, and fruit of plants.
•Allows the rows between plants to remain dry, improving access and reducing weed growth.
•Saves time, money, and water because the system is so efficient.
•Decreases labor.
•Increases effectiveness on uneven ground.
•Reduces leaching of water and nutrients below the root zone.
4.3 According to type of operation. the emitting pipes shall be classified into the following two classes:
1. Regulated Emitting Pipe
2. Un-regulated Emitting Pipe
Regulated Emitting Pipe : Regulated (Pressure Compensating) Emitting Pipe—
Emitting pipe of relatively constant emission rate at varying water pressure levels at
the emitting pipe inlet, within the range of operating pressure specified by the
manufacturer.
Example:
Emitting pipe IS 13488 16-2-1-x-PC-A designates a emitting pipe complying with this Indian Standard.
of 16mm nominal outside diameter.2l/h emission rate. with working pressure 0.100 Mpa (class 1).
emitter spacing. regulated(pressure compensated) and confirming to uniformity Category A
• Un-regulated Emitting Pipe : Unregulated Emitting Pipes. Measure the emission rates of the
emitting units in the emitting pipes, when the water pressure at the inlets of the emitting units
equals the nominal test pressure.
Example:
Emitting pipe IS 13488 16-2-1-x-A designates a emitting pipe complying with this Indian
Standard. of 16mm nominal outside diameter.2l/h emission rate. with working pressure 0.100
Mpa (class I). emitter spacing. non-regulated and confirming to uniformity Category A.
Test Result as per IS 13488 - 2008
Sr No Clause No. Test Test Method Unit Specified Requirements
1 5.1.2 Carbon Black content IS : 2530 % 2.5 ± 0.5%
2 Carbon Black Dispersion Should be satisfactory
3 6.2 Fittings IS : 13488 - 2008 Fittings suitable in size, shape and sufficient strength to withstand the full range of
working pressure
4 6.3 General IS : 13488 - 2008 Pipe and fitting shall have no manufacturing defect & permit easy connection
5 8.1 Uniformity of emission rate at
(Pn) Mean Emission Rate
IS : 13488 - 2008 LPH LPH
a) CV % % Max. 5% / 10%
b) Mean deviation of emission
rate %
% Max. 5% / 10%
6 8.2 Emission rate at function inlet pressure % deviation at Category – A, ± 5%
/ Category –B, ± 10%
i) Kg/cm² IS : 13488 - 2008 LPH LPH
ii) Kg/cm²
iii) Kg/cm² LPH
iv) Kg/cm² LPH
v) Kg/cm² LPH
Percentage deviation at emission rate
i) Kg/cm² IS : 13488 - 2008 % Max. 5% / 10%
ii) Kg/cm² Max. 5% / 10%
iii) Kg/cm² Max. 5% / 10%
iv) Kg/cm² Max. 5% / 10%
v) Kg/cm² Max. 5% / 10%
Sr. No. Clause No Test Testing Method Unit Specified Requirement
7 8.3 Dimension IS : 13488 – 2008 mm
8.3.1 Wall Thickness
Min.
Max.
8.3.2 Diameter (Internal)
8.3.3 Flow Path Min.
8.3.4 Spacing of Emitting Unit mm ± 5.0%
8 8.4.1 Resistance of Emitting Pipe to Hydraulic Pressure
a) 1.8 times of max. working pressure IS : 13488 - 2008 --------- No sign of leakage & shall not pull a part
b) Flow rate as per CI. 8.1 (%) % Max. 10%
9 8.4.2 Resistance of Emitting Pipe to Hydraulic Pressure at Elevated temperature
a) Working Pressure P Max. IS : 13488 - 2008 ------- Shall withstand the pressure without showing
signs of damage
b) Flow rate as per CI. 8.1 (%) % Max. 10%
10 8.5 Resistance to Tension at Elevated Tempereture
a)---------N for 15 Minutes IS : 13488 - 2008 ------- Shall withstand the test pull without breaking or
tearing
b) Flow rate as per CI. 8.1 (%) % Max. 5%
c) Distance between 2 marking (%) % Max. 5%
11 8.6 Resistance to pill out of joints between fittings &
emitting pipe
IS : 13479 -------- Shall withstand the pulling for -----N for 1 Hrs.
12 8.7 Resistance to ESCR The pipe is considered to have passed the test
is not more than 10% of the bends ( that is 0 out
of 10 or 2 out of 20) have failed
8.7.1 Acceptance test ( 77°C 1 Hrs.) IS : 12786 -----
8.7.2 Type Test (77°C 48 Hrs.)
13 8.8 Emitting Unit Exponent IS : 13488 - 2008 ------- Shall be less than 0.5
1 SCOPE
This standard specifies the mechanical and functional requirements of the emitting pipes
and their fittings, test methods and the data to be supplied by the manufacturer to
facilitate correct installation and operation in the field.
2 REFERENCES
The following standards contain provisions, which through reference in this text,
constitute provisions of this standard. At the time of publication, the editions indicated
were valid. All standards are subject to revision and parties to agreements based on this
standard are encouraged to investigate the possibility of applying the most recent
editions of the standards indicated below:
IS No. Title
12786: 1989 Polyethylene pipes for irrigation laterals
13479: 1992 Assembled joints between fittings and polyethylene pressure pipes – Test
of resistance to pull out.
3 TERMINOLOGY
For the purpose of this standard the following definitions shall apply.
3.1 Clamping Band/Ring - A ring like or a band like device used for tightening the joints between
emitting pipe and fittings.
3.2 Emitter/Emitting Unit Exponent (m? - Numerical value that defines the exponential
relationship between the emission rate and inlet pressure of an emitting unit.
3.3 Emitting Pipe - Continuous pipe, hose or tubing with perforation or other hydraulic devices,
formed or integrated in the pipe, hose or tubing during production and intended to emit water in
the form of drops or continuous flow, at nominal emission rates not exceeding 8 l/h per emitting
unit at nominal test pressure.
3.4 Emitting Unit - A section of emitting pipe, including all its hydraulic devices formed or
integrated in the pipe during production and all of the emitter inlets, repeated at intervals from
which water is emitted to one clearly distinguishable location.
3.5 Fitting - Any connecting device suitable for attachment to the emitting pipe with or without
clamping band.
3.6 Inlet Fitting - Fitting having one end suitable for connection to a standard irrigation lateral or
appliance and other end or ends suitable for connecting to an emitting pipe.
3.7 In line Fitting - Fitting with both ends suitable for connection to an emitting pipe.
3.8 Maximum Working Pressure - Highest water pressure at the inlet of an emitter/emitting pipe
recommended by the manufacturer to ensure proper functioning of the emitter/emitting pipe.
3.9 Minimum Working Pressure - Lowest working pressure at the inlet of an emitter/emitting unit
recommended by the manufacturer to ensure proper functioning of the emitter/emitting pipe.
3.10 Nominal Diameter - Conventional numerical designation used to indicate the size of the
emitting pipe and approximately equal to the outside diameter (in millimeters) of the pipe. 3.11
Nominal Emission Rate (Qn)
3.11.1 Unregulated (Non-pressure Compensating) Emitting Pipe - The emission rate, in liters per hour,
of the emitting unit at nominal test pressure and at a water temperature of 27 ± 3°e as specified by the
manufacturer.
3.11.2 Regulated (Pressure Compensating) Emitting Pipe - The emission rate, in liters per hour. of the
emitting unit operating in the range of regulation and at a water temperature of 27 ± 3°e as specified by
the manufacturer.
3.12 Nominal Test Pressure (Pn) - A reference pressure of 100 kPa at the inlet of an unregulated
emitting unit, or any other pressure specified in the publication of the manufacturer as 'nominal test
pressure’
3.13 Range of Working Pressure - The range of water pressures at the inlet of the regulated emitting
unit. between and including the minimum working pressure (PMin) and the maximum working pressure
(PM••) recommended by the emitting pipe manufacturer to ensure proper functioning.
3.14 Range of Regulation - The range of water pressure at the inlet of the regulated emitting unit. in
which each emitting unit of the emitting pipe discharges water within the range of emission rates
specified by the manufacturer
3.15 Regulated (Pressure Compensating) Emitting Pipe - Emitting pipe of relatively constant emission
rate at varying water pressure levels at the emitting pipe inlet. within the range of operating pressure
specified by the manufacturer.
3.16 Spacing of Emitters/Emitting Units Distance between two successive emitters/emitting units
integrated inside the emitting pipe.
3.17 Unit Emitting Pipe - Length of an emitting pipe containing one emitting unit.
3.18 Unregulated Emitting Pipe - Emitting pipe whose emission rate varies with inlet water pressure
4 CLASSIFICATION
4.1 Emitting pipe shall be classified according to their uniformity of emission rate and regulation. into
the following two uniformity categories.
4.1.1 Uniformity Category A Emitting pipe having higher uniformity of emission rates and smaller
deviations from the specified nominal emission rate.
4.1.2 Uniformity Category B Emitting pipes having lower uniformity of emission rates and greater
deviations from the specified nominal emission rate.
4.2 The emitting pipes shall be classified by pressure ratings (working pressure) as follows:
Class of Pipe Working Pressure
Class I 0.100
Class 2 0.125
Class 3 0.250
Class 4 0.400
10. DETERMINATION OF CARBON BLACK CONTENT
Introduction :
Carbon black is mainly used to strengthen rubber in tires, but can also act as a pigment, UV stabilizer, and
conductive or insulating agent in a variety of rubber, plastic, ink and coating applications.
10.1 Apparatus
Combustion Boat - made of porcelain or silica, having minimum dimensions of 75 mm length, 9 mm width and 8 mm
height.
Combustion Tube - made of hard glass, of approximately 30 mm diameter and 400 f: 50 mm length.
Gas Flow Meter-for measuring and controlling the rate of 5ow of nitrogen within 1.7 * 03 liters per minute.
Thermometer - in the range 250” to 550°C.
Furnace - to accommodate the combustion tube and to give temperatures up to at least 5OO’C.
Reagents
Nitrogen - gas and Trichloroethylene
TEST SAMPLE:
About 1 gm of sample cut into small pieces are used
Procedure :
 Heat the combustion boat to red heat, allow it to cool in a desiccator for at least 30 minutes and
weigh to the nearest 0.001 gm.
 Place about 1 g of the sample, accurately weighed, in the boat.
 Place the boat with the sample in the middle of the combustion tube. Insert a stopper carrying a
thermometer and a tube for the admission of nitrogen into one end of the combustion tube.
 Pass nitrogen through the combustion tube at a rate of I.7 f 0.3 liters per minute and maintain the
same rate of flow during through subsequent heating.
 Place the combustion tube in the furnace and connect its outlet to two cold traps in series, both
containing trichloroethylene and the first being cooled with solid carbon dioxide.
 Put the outlet tube from the second trap to a fume hood or to the outside atmosphere.
 Heat the furnace to 500±5°C and maintain this temperature for 10 minutes.
 Disconnect the outlet tube from the cold traps. Withdraw the combustion tube containing the boat
from the furnace and allow to cool for 5 minutes, maintaining the flow of nitrogen at the same rate as
before.
 Remove the boat from the nitrogen inlet side of the combustion tube, allow it to cool in the desiccator
for 20 to 30 minutes and weigh to the nearest 0.001 g ( W, ). Heat the boat strongly in air to constant
weight ( W, ).
Calculation
Carbon black content, percent by weight = 100 ×
𝑤1−𝑤2
𝑤3
where W1= weight in g of the boat before heating in air,
W2= weight in g of the boat after heating in air, and
W3 = weight in g of the material taken for the test.
DETERMINATION OF CARBON BLACK DISPERSION IN POLYETHYLENE MATERIALS
Procedure
• Place two clean microscope slides on a hot plate maintained at
170” to 210°C. Place three specimens of pin-head size, each
weighing about 5 mg, and each one cut from a separate granule, on
one of the hot microscope slides, about 20 mm apart. Place a piece
of metal shim 40 mm long, 20 mm wide and 0.03 mm thick at each
end and cover the whole with the other hot microscope slide. Press
the specimens by applying even pressure for I$ to 2 minutes, to the
whole area of the face of the upper slide. After the specimens have
been placed on the slides, these shall not remain on the hot plate
for more than 3 minutes.
• When the slides are cool enough to be handled, examine the three
specimens through a microscope at a magnification of 200 f. 10
with a field of view of 1 3: 0.1 mm diameter. Compare each
specimen with the photomicrograph shown in Fig. 5 in respect of
number and size of agglomerates. Note : also be made of any lack
of uniformity of the background.
6.2 Fittings
6.2.1 The manufacturer shall supply, for each type and size of emitting pipe, fittings
suitable in size and shape to make good connections to the emitting pipe.
6.2.2 The jointing, made with or without the use of clamping bands. shall be of
sufficient strength to withstand the full range of working pressure.
6.3 General
The emitting pipe. its parts and fittings, shall have no manufacturing defects that may
impair their performance. The construction of the emitting pipe and its fittings shall
permit their easy connection, with or without clamping bands/rings, whether the
connection is made manually or by means of suitable tools supplied by the
manufacturer.
8.1 Uniformity of Emission Rate
8.1.1 This test applies to regulated as well as to unregulated emitting pipe. The test
sample shall include at least 25 emitting units in accordance with that specified in 7.1.
8.1.2 Unregulated Emitting Pipes
Measure the emission rates of the emitting units in the emitting pipes. when the water
pressure at the inlets of the emitting units equals the nominal test pressure. Record
separately the measured emission rate of each emitting outlet.
Calculate the coefficient of variation. Cv from the following formula:
C =
𝑠𝑞
𝑞
× 100
where, Sq = standard deviation of the emission rates for the sample, and
q = mean emission rate of sample.
8.1.2.1The mean emission rate of the test sample shall not deviate from the nominal emission rate(qn)by more than 5
percent for Category A, or not more than 10 percent for Category B in accordance with Table 2.
Table 2 Uniformity Values
[Clauses 8.1.2.1 and l Itd)]
Sl No Category Deviation of q from qx, max Coefficient of variation Cv
(1) (2) (3) (4)
i) A 5 5
ii) B 10 10
8.1.2.2 The co-efficient of variation (C) of the emission rate of the test sample shall not exceed 5 percent for Category
A, or 10 percent for Category B.
8.1.3 Regulated Emitting Pipes Condition the emitting units in the test sample by operating them for one hour minimum
at an emitting unit with inlet pressure equal to the pressure at the middle of the working pressure range. At the
beginning of conditioning, the emitting units shall be operated three times at about Pmax and three times at about
Pmin each operation to be maintained for at least three minutes. During the last 10 min of conditioning, the pressure
shall be maintained at the midpoint of the range of regulation. Immediately after, and without altering the inlet pressure,
test the emitting units according to 8.1.2 but at the midpoint of the range of regulation.
8.1.3.1 The emitting units shall comply with the requirements given in 8.1.2.1 and 8.1.2.2.
8.2Emission Rate of Emitting Unit as a Function of Inlet Pressure
Number the emitting units tested according to 7.1, in ascending order according to the measured
emission rate.(No. I shall be given to the emitting unit of lowest emission rateandNo.25 to the emitting
units of highest emission rate). Select4 emitting units from the series obtained, No.3, 12, 13,23 and
measure their change in emission rate as a function of the inlet pressure. Test each emitting unit in steps
not greater than 50 kPa, from Pmin Up to 1.2Pmax Regulated emitting units shall be tested at three or
more different pressures within the range of regulation, at rising and falling inlet pressure. The reading of
the results shall be taken at least three minutes after arriving at the test pressure. If the inlet pressure
exceeds the desired pressure by more than 10kPaduring its rise and fall, return to •Pmin and repeat the
test.
8.2.1 Unregulated Emitting Pipe
Calculate for each pressure value, the average emission rate q obtained by measuring the emission rate
of the four emitting units at rising pressure.
Plot the curve q as function of inlet pressure.
8.2.1.1 The curve of q shall conform to the curve presented in the publication of the manufacturer within
an allowable deviation of not more than±5 percent for Category A and ±1O percent for Category B.
8.2.2 Regulated Emitting Pipes
Calculate for each inlet pressure value , Pi the average emission rate q obtained by measuring the emission rate of
the four emitting units at rising and falling pressure(the average of 8 emission rate measurement).
8.2.2.1 The value of q shall not deviate from the nominal emission rate by more than 5 percent for Category A or
not more than 10 percent for Category B.
8.3 Dimensions
8.3.1 Wall Thickness of Emitting Pipe Measure the wall thickness of the emitting pipe at four points equally spaced
on the periphery of the pipe. Repeat the test at two cross sections. In the event of a part the pipe wall being thicker
by design(for example, flap in emitting pipe), such increase in thickness shall be disregarded.
8.3.1.1 The wall thickness of the emitting pipe, when measured at each of the four points, shall be within limits given
in Table 1.
8.3.2 Inside Diameter of Emitting Pipe
For measuring the inside diameter of emitting pipe, insert into the end of the pipe a specific taper gauge
(with2°apexangle)or 'Go', 'No-Go’ gauge , first enter GO side of the gauge, it should go inside the tube without much
force but at the same time it should not remain loose in the tube. For example a GO, NO-GO gauge sketch is given
at Fig. 1 for 16 mm nominal diameter tube. Alternatively the outside diameter may be measured with pie tape or
vernier caliper, from which two times the average thickness measured at the same point of pipe can be deducted to
obtain the inside diameter.
8.3.2.1 The measured inside diameter shall be within the limits given in Table .
8.3.3 Flow Paths in Emitting Unit
Measure in at least three emitting units, accurately to the nearest 0.02 mm and under
no pressure, the smallest dimension of the flow path (this does not apply to dimension
that varies with pressure).
8.3.3.1 The smallest measured flow path dimension shall not be smaller than the
dimensions declared by the manufacturer.
8.3.4 Spacing of Emitter Units
Measure three spacings of emitting units, accurately to the nearest 1.0 mm.
8.3.4.1 The spacing of the emitting units shall not deviate by more than 5 percent from
the spacings declared by the manufacturer.
8.4 Resistance of Emitting Pipes to Hydrostatic Pressure
8.4.1 Resistance to Hydrostatic Pressure at Ambient Temperature Perform the test on a length
of emitting pipe consisting of five unit emitting pipes joined by means of center fittings.
Perform this test in two stages(see 8.4.1.1 and8.4.1.2).
8.4.1.1Connect the emitting pipe assembly to a source of water, by means of an inlet fitting,
and close its outlet end. Fill the emitting pipe assembly with water and check that no air
remains trapped in the pipe. Increase the water pressure gradually (10 s, Min) to the maximum
working pressure multiplied by 1.8 and maintain the test pressure for 1 h.
The emitting pipe assembly shall withstand the test pressure without showing signs of damage
to the emitting pipe, the emitting units or the connecting fittings. The unit emitting pipes shall
not pull apart, and no leakage shall occur at the inlet fitting. Leakages not exceeding the
emission rate of one emitting unit are permissible at center fittings.
8.4.1.2 Reduce the test pressure to nominal pressure and maintain for at least 3 min. Measure the flow
rate of each emitting unit.
The flow rate of each emitting unit shall not deviate by more than 10 percent from its initially observed
flow rate, as measured in 8.1.
8.4.2 Resistance to Hydrostatic Pressure at Elevated Temperature
Perform the teston a length of emitting pipe consisting of 3 emitting-pipe units jointed by means of center
fittings. Perform the test in two stages (see 8.4.2.1 and8.4.2.2).
8.4.2.1Connect the emitting-pipe assembly to a source of water, by means of an inlet fitting, and close its
outlet end. Fill the emitting-pipe assembly with water and check that no air remains trapped in the pipe.
Raise the water pressure gradually (10 s, Min) to maximum pressure and maintain the pressure for 48 h,
while the emitting-pipe test assembly is immersed in water at 60:1: 2°C temperature.
The emitting pipe shall withstand the test pressure without showing signs of damage.
8.4.2.2 Remove the test assembly from the water and maintain it for 30
min at ambient temperature. Apply a hydrostatic pressure Pn for at least 3
min at ambient temperature and measure the flow rate of each emitting
unit.
The flow rate of each emitting unit shall not deviate by more than 10
percent from its original flow rate, as measured in 8.1.
8.S Resistance to Tension at Elevated Temperature
Perform the test on 5 unit emitting pipe at a temperature of 50:1: 2°C.
NOTE- Mark on the unit emitting pipe two lines about 150 mm apart. Fasten
one end of the emitting pipe in an air circulation oven maintained at 50 :t 2"C and
apply a dead weight in accordance with Table 3. Maintain the pull for 15 min. then
remove the pull and cool the unit emitting pipe to an ambient temperature.
8.5.1Emitting pipe shall withstand the test pull without breaking or tearing. The
nominal flow rate in the test specimen shall not vary by more than 5 percent from
the flow rate measured before testing according to 8.1, and the distance between
the two marked lines shall not vary by more than 5 percent from the distance
measured (see 8.5)
8.6 Resistance to Pull Out of Joints Between Fitting and Emitting
This test shall be performed in accordance with IS 13479, but the test pull out load shall be
according to Table3, applied for 1 hr or alternatively dead weight may be used for applying the test
pull. The fitting shall not pull out from the emitting pipe.
PRINCIPLE
Checking of the ability of an
assembled joint to resist pulling out
when submitted to longitudinal
tension.
3 APPARATUS
Tensometer capable of holding the
test specimen at a constant
longitudinal stress .
the design for jointing O pipe with
ding 63 mm Alternatively, the
calculated force may be applied to
the specimen by means of weights,
in which case the specimen shall
be suspended on a frame with a
suitable stirrup at the lower end of
the specimen to hold the weights.
• Resistance to ESCR :
• 8.7.1 Acceptance Test (77°C & 1 Hr)
• The test procedure shall conform to the procedure described in Annex D of IS 12786, except for the
following: Condition the test specimen in an air circulating oven at 80:1: l°C for 1 h.
• Then air cool and U bend the specimen and immerse in a constant temperature bath. Containing the
reagent.
• Percentage concentration = 10 percent of surface active agent
• Test temperature = 77 ± 3°C
• Test duration = 1 Hr
• Reagent = Nonyl Phenoxy polyethyleneoxy ethanol ( Igepal CO-630)
• Specimen size = 38 x 13 mm
• 8.7.2 Type Test
• The test procedure shall confirm to the procedure described in Annex D of IS 12786.except for the test
temperature and test duration which shall be as specified below:
• Percentage concentration = 10 percent of surface active agent
• Test temperature = 77 ± 3°C
• Test duration = 48 h
• Reagent = Nonyl Phenoxy polyethyleneoxy ethanol ( Igepal CO-630)
• Specimen size = 38 x 13 mm
TEST METHOD
D-2.1 Reagent An undiluted surface active agent of the type of
nonylphenoxy poly ( ethyleneoxy ) ethanol [ Igepal CO-630 or
Antarox CO-6301 may be used for reference purposes. This
information is given for the convenience of users and does not
constitute endorsement of the product kept in closed containers
and used fresh for each test.
D-2.2 Apparatus
Forced air circulation oven, maintained at 50 ± 3°C, capable of
re-establishing that temperature within five minutes after insertion
of test pieces.
D-2.3 Test Specimen
Five sections of pipe, preferably from different coils, each of
length about 20 times the diameter shall constitute the test piece.
D-2.4 Procedure
D-2.4.1 Bend each test piece sharply at two pieces, to form two U-bends, in two different planes
perpendicular to each other (see fig -2 ).Each bend is worked to the limit , that is until both sides of the fold
touch and lie parallel to each other, and then the bend is tightly secured to maintain that deformation
throughout the test ( see Fig. 2 ).
D-2.4.2 Coat each bend completely with the reagent by dipping and then place all the test pieces in the
oven, taking care not to impose any additional stresses on them.
-D-2.4.3 30 minutes after the temperature of the oven ( bath ) has returned to 50 f 3% take the test pieces
out and release the stress and wipe the bends free from reagent.
D-2.4.4 Inspect each bend thoroughly, with the unaided eye for any visible cracks ( generally originating at
the two ends of the fold).
D-2.5 Expression of Results
Any bend which contains at least one visible crack (-excluding cracks induced by the object used to secure
the bend ), is classified as failed. The total number of bends which fail shall be noted.
8.8 Determination of Emitting Unit Exponent (This Test Applies to Both Regulated and Unregulated Emitting Units)
The relation between the emission rate. 𝑞. in 1/h and the inlet pressure in an emitting unit .P. in kilopascals, is
given by the formula:
𝑞 = 𝑘 ⋅ 𝑝𝑚
m =
𝐥𝐨𝐠 𝒑𝒊 𝐥𝐨𝐠 𝒒ⅈ −𝟏
𝒏 𝜮 𝐥𝐨𝐠 𝒑𝒊 𝐥𝐨𝐠 𝒒ⅈ
𝐥𝐨𝐠 𝒑𝒊
𝟐−𝟏
𝒏 𝐥𝐨𝐠 𝒑𝒊
𝟐
where q =emission rate. in 1/h;
k =constant;
p = inlet pressure. in KPa;
m =emitting unit exponent;
i= 1.2.3.4.......... n; and
n = number of pressure values used in 8.2.2.
Using all the q and p values obtained in 8.2.2.calculate m from the above formula.
The value of the emitting unit exponent m shall be less than0.5 for non-regulated emitting pipes and less than
0.2 for regulated emitting pipes.
THANK YOU

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tushar is - 13488.pptx

  • 1. IS 13488 - 2008 IRRIGATION EQUIPMENT– EMITTING PIPE SYSTEM SUBMITTEDTO– JAGANS. MEHTASIR SUBMITTEDBY – TUSHARRANJANSARKAR COURSE– PGD-PPT3RD SEMESTER ROLL NO. - 220106017
  • 2. What is Emitting Pipe ? Emitting Pipe play a key role in drip irrigation systems. Emitting pipes are manufactured from virgin special grade polyethylene. Resistant to Ultra Violet (UV) radiation and other environmental effects . Emitting Pipe passes through stringent quality tests confirming to Indian and International Standards .The nominal diameter ranges from 12 mm to 25 mm.
  • 3. Benefits of Drip Irrigation Drip irrigation involves placing tubing with emitters on the ground along side the plants. The emitters slowly drip water into the soil at the root zone. Because moisture levels are kept at an optimal range, plant productivity and quality improve. In addition, drip irrigation: •Prevents disease by minimizing water contact with the leaves, stems, and fruit of plants. •Allows the rows between plants to remain dry, improving access and reducing weed growth. •Saves time, money, and water because the system is so efficient. •Decreases labor. •Increases effectiveness on uneven ground. •Reduces leaching of water and nutrients below the root zone.
  • 4. 4.3 According to type of operation. the emitting pipes shall be classified into the following two classes: 1. Regulated Emitting Pipe 2. Un-regulated Emitting Pipe Regulated Emitting Pipe : Regulated (Pressure Compensating) Emitting Pipe— Emitting pipe of relatively constant emission rate at varying water pressure levels at the emitting pipe inlet, within the range of operating pressure specified by the manufacturer. Example: Emitting pipe IS 13488 16-2-1-x-PC-A designates a emitting pipe complying with this Indian Standard. of 16mm nominal outside diameter.2l/h emission rate. with working pressure 0.100 Mpa (class 1). emitter spacing. regulated(pressure compensated) and confirming to uniformity Category A
  • 5. • Un-regulated Emitting Pipe : Unregulated Emitting Pipes. Measure the emission rates of the emitting units in the emitting pipes, when the water pressure at the inlets of the emitting units equals the nominal test pressure. Example: Emitting pipe IS 13488 16-2-1-x-A designates a emitting pipe complying with this Indian Standard. of 16mm nominal outside diameter.2l/h emission rate. with working pressure 0.100 Mpa (class I). emitter spacing. non-regulated and confirming to uniformity Category A.
  • 6. Test Result as per IS 13488 - 2008 Sr No Clause No. Test Test Method Unit Specified Requirements 1 5.1.2 Carbon Black content IS : 2530 % 2.5 ± 0.5% 2 Carbon Black Dispersion Should be satisfactory 3 6.2 Fittings IS : 13488 - 2008 Fittings suitable in size, shape and sufficient strength to withstand the full range of working pressure 4 6.3 General IS : 13488 - 2008 Pipe and fitting shall have no manufacturing defect & permit easy connection 5 8.1 Uniformity of emission rate at (Pn) Mean Emission Rate IS : 13488 - 2008 LPH LPH a) CV % % Max. 5% / 10% b) Mean deviation of emission rate % % Max. 5% / 10% 6 8.2 Emission rate at function inlet pressure % deviation at Category – A, ± 5% / Category –B, ± 10% i) Kg/cm² IS : 13488 - 2008 LPH LPH ii) Kg/cm² iii) Kg/cm² LPH iv) Kg/cm² LPH v) Kg/cm² LPH Percentage deviation at emission rate i) Kg/cm² IS : 13488 - 2008 % Max. 5% / 10% ii) Kg/cm² Max. 5% / 10% iii) Kg/cm² Max. 5% / 10% iv) Kg/cm² Max. 5% / 10% v) Kg/cm² Max. 5% / 10%
  • 7. Sr. No. Clause No Test Testing Method Unit Specified Requirement 7 8.3 Dimension IS : 13488 – 2008 mm 8.3.1 Wall Thickness Min. Max. 8.3.2 Diameter (Internal) 8.3.3 Flow Path Min. 8.3.4 Spacing of Emitting Unit mm ± 5.0% 8 8.4.1 Resistance of Emitting Pipe to Hydraulic Pressure a) 1.8 times of max. working pressure IS : 13488 - 2008 --------- No sign of leakage & shall not pull a part b) Flow rate as per CI. 8.1 (%) % Max. 10% 9 8.4.2 Resistance of Emitting Pipe to Hydraulic Pressure at Elevated temperature a) Working Pressure P Max. IS : 13488 - 2008 ------- Shall withstand the pressure without showing signs of damage b) Flow rate as per CI. 8.1 (%) % Max. 10% 10 8.5 Resistance to Tension at Elevated Tempereture a)---------N for 15 Minutes IS : 13488 - 2008 ------- Shall withstand the test pull without breaking or tearing b) Flow rate as per CI. 8.1 (%) % Max. 5% c) Distance between 2 marking (%) % Max. 5% 11 8.6 Resistance to pill out of joints between fittings & emitting pipe IS : 13479 -------- Shall withstand the pulling for -----N for 1 Hrs. 12 8.7 Resistance to ESCR The pipe is considered to have passed the test is not more than 10% of the bends ( that is 0 out of 10 or 2 out of 20) have failed 8.7.1 Acceptance test ( 77°C 1 Hrs.) IS : 12786 ----- 8.7.2 Type Test (77°C 48 Hrs.) 13 8.8 Emitting Unit Exponent IS : 13488 - 2008 ------- Shall be less than 0.5
  • 8. 1 SCOPE This standard specifies the mechanical and functional requirements of the emitting pipes and their fittings, test methods and the data to be supplied by the manufacturer to facilitate correct installation and operation in the field. 2 REFERENCES The following standards contain provisions, which through reference in this text, constitute provisions of this standard. At the time of publication, the editions indicated were valid. All standards are subject to revision and parties to agreements based on this standard are encouraged to investigate the possibility of applying the most recent editions of the standards indicated below: IS No. Title 12786: 1989 Polyethylene pipes for irrigation laterals 13479: 1992 Assembled joints between fittings and polyethylene pressure pipes – Test of resistance to pull out.
  • 9. 3 TERMINOLOGY For the purpose of this standard the following definitions shall apply. 3.1 Clamping Band/Ring - A ring like or a band like device used for tightening the joints between emitting pipe and fittings. 3.2 Emitter/Emitting Unit Exponent (m? - Numerical value that defines the exponential relationship between the emission rate and inlet pressure of an emitting unit. 3.3 Emitting Pipe - Continuous pipe, hose or tubing with perforation or other hydraulic devices, formed or integrated in the pipe, hose or tubing during production and intended to emit water in the form of drops or continuous flow, at nominal emission rates not exceeding 8 l/h per emitting unit at nominal test pressure. 3.4 Emitting Unit - A section of emitting pipe, including all its hydraulic devices formed or integrated in the pipe during production and all of the emitter inlets, repeated at intervals from which water is emitted to one clearly distinguishable location.
  • 10. 3.5 Fitting - Any connecting device suitable for attachment to the emitting pipe with or without clamping band. 3.6 Inlet Fitting - Fitting having one end suitable for connection to a standard irrigation lateral or appliance and other end or ends suitable for connecting to an emitting pipe. 3.7 In line Fitting - Fitting with both ends suitable for connection to an emitting pipe. 3.8 Maximum Working Pressure - Highest water pressure at the inlet of an emitter/emitting pipe recommended by the manufacturer to ensure proper functioning of the emitter/emitting pipe. 3.9 Minimum Working Pressure - Lowest working pressure at the inlet of an emitter/emitting unit recommended by the manufacturer to ensure proper functioning of the emitter/emitting pipe. 3.10 Nominal Diameter - Conventional numerical designation used to indicate the size of the emitting pipe and approximately equal to the outside diameter (in millimeters) of the pipe. 3.11 Nominal Emission Rate (Qn)
  • 11. 3.11.1 Unregulated (Non-pressure Compensating) Emitting Pipe - The emission rate, in liters per hour, of the emitting unit at nominal test pressure and at a water temperature of 27 ± 3°e as specified by the manufacturer. 3.11.2 Regulated (Pressure Compensating) Emitting Pipe - The emission rate, in liters per hour. of the emitting unit operating in the range of regulation and at a water temperature of 27 ± 3°e as specified by the manufacturer. 3.12 Nominal Test Pressure (Pn) - A reference pressure of 100 kPa at the inlet of an unregulated emitting unit, or any other pressure specified in the publication of the manufacturer as 'nominal test pressure’ 3.13 Range of Working Pressure - The range of water pressures at the inlet of the regulated emitting unit. between and including the minimum working pressure (PMin) and the maximum working pressure (PM••) recommended by the emitting pipe manufacturer to ensure proper functioning.
  • 12. 3.14 Range of Regulation - The range of water pressure at the inlet of the regulated emitting unit. in which each emitting unit of the emitting pipe discharges water within the range of emission rates specified by the manufacturer 3.15 Regulated (Pressure Compensating) Emitting Pipe - Emitting pipe of relatively constant emission rate at varying water pressure levels at the emitting pipe inlet. within the range of operating pressure specified by the manufacturer. 3.16 Spacing of Emitters/Emitting Units Distance between two successive emitters/emitting units integrated inside the emitting pipe. 3.17 Unit Emitting Pipe - Length of an emitting pipe containing one emitting unit. 3.18 Unregulated Emitting Pipe - Emitting pipe whose emission rate varies with inlet water pressure
  • 13. 4 CLASSIFICATION 4.1 Emitting pipe shall be classified according to their uniformity of emission rate and regulation. into the following two uniformity categories. 4.1.1 Uniformity Category A Emitting pipe having higher uniformity of emission rates and smaller deviations from the specified nominal emission rate. 4.1.2 Uniformity Category B Emitting pipes having lower uniformity of emission rates and greater deviations from the specified nominal emission rate. 4.2 The emitting pipes shall be classified by pressure ratings (working pressure) as follows: Class of Pipe Working Pressure Class I 0.100 Class 2 0.125 Class 3 0.250 Class 4 0.400
  • 14. 10. DETERMINATION OF CARBON BLACK CONTENT Introduction : Carbon black is mainly used to strengthen rubber in tires, but can also act as a pigment, UV stabilizer, and conductive or insulating agent in a variety of rubber, plastic, ink and coating applications. 10.1 Apparatus Combustion Boat - made of porcelain or silica, having minimum dimensions of 75 mm length, 9 mm width and 8 mm height. Combustion Tube - made of hard glass, of approximately 30 mm diameter and 400 f: 50 mm length. Gas Flow Meter-for measuring and controlling the rate of 5ow of nitrogen within 1.7 * 03 liters per minute. Thermometer - in the range 250” to 550°C. Furnace - to accommodate the combustion tube and to give temperatures up to at least 5OO’C. Reagents Nitrogen - gas and Trichloroethylene TEST SAMPLE: About 1 gm of sample cut into small pieces are used
  • 15. Procedure :  Heat the combustion boat to red heat, allow it to cool in a desiccator for at least 30 minutes and weigh to the nearest 0.001 gm.  Place about 1 g of the sample, accurately weighed, in the boat.  Place the boat with the sample in the middle of the combustion tube. Insert a stopper carrying a thermometer and a tube for the admission of nitrogen into one end of the combustion tube.  Pass nitrogen through the combustion tube at a rate of I.7 f 0.3 liters per minute and maintain the same rate of flow during through subsequent heating.  Place the combustion tube in the furnace and connect its outlet to two cold traps in series, both containing trichloroethylene and the first being cooled with solid carbon dioxide.  Put the outlet tube from the second trap to a fume hood or to the outside atmosphere.  Heat the furnace to 500±5°C and maintain this temperature for 10 minutes.  Disconnect the outlet tube from the cold traps. Withdraw the combustion tube containing the boat from the furnace and allow to cool for 5 minutes, maintaining the flow of nitrogen at the same rate as before.  Remove the boat from the nitrogen inlet side of the combustion tube, allow it to cool in the desiccator for 20 to 30 minutes and weigh to the nearest 0.001 g ( W, ). Heat the boat strongly in air to constant weight ( W, ).
  • 16. Calculation Carbon black content, percent by weight = 100 × 𝑤1−𝑤2 𝑤3 where W1= weight in g of the boat before heating in air, W2= weight in g of the boat after heating in air, and W3 = weight in g of the material taken for the test.
  • 17. DETERMINATION OF CARBON BLACK DISPERSION IN POLYETHYLENE MATERIALS Procedure • Place two clean microscope slides on a hot plate maintained at 170” to 210°C. Place three specimens of pin-head size, each weighing about 5 mg, and each one cut from a separate granule, on one of the hot microscope slides, about 20 mm apart. Place a piece of metal shim 40 mm long, 20 mm wide and 0.03 mm thick at each end and cover the whole with the other hot microscope slide. Press the specimens by applying even pressure for I$ to 2 minutes, to the whole area of the face of the upper slide. After the specimens have been placed on the slides, these shall not remain on the hot plate for more than 3 minutes. • When the slides are cool enough to be handled, examine the three specimens through a microscope at a magnification of 200 f. 10 with a field of view of 1 3: 0.1 mm diameter. Compare each specimen with the photomicrograph shown in Fig. 5 in respect of number and size of agglomerates. Note : also be made of any lack of uniformity of the background.
  • 18. 6.2 Fittings 6.2.1 The manufacturer shall supply, for each type and size of emitting pipe, fittings suitable in size and shape to make good connections to the emitting pipe. 6.2.2 The jointing, made with or without the use of clamping bands. shall be of sufficient strength to withstand the full range of working pressure. 6.3 General The emitting pipe. its parts and fittings, shall have no manufacturing defects that may impair their performance. The construction of the emitting pipe and its fittings shall permit their easy connection, with or without clamping bands/rings, whether the connection is made manually or by means of suitable tools supplied by the manufacturer.
  • 19. 8.1 Uniformity of Emission Rate 8.1.1 This test applies to regulated as well as to unregulated emitting pipe. The test sample shall include at least 25 emitting units in accordance with that specified in 7.1. 8.1.2 Unregulated Emitting Pipes Measure the emission rates of the emitting units in the emitting pipes. when the water pressure at the inlets of the emitting units equals the nominal test pressure. Record separately the measured emission rate of each emitting outlet. Calculate the coefficient of variation. Cv from the following formula: C = 𝑠𝑞 𝑞 × 100 where, Sq = standard deviation of the emission rates for the sample, and q = mean emission rate of sample.
  • 20. 8.1.2.1The mean emission rate of the test sample shall not deviate from the nominal emission rate(qn)by more than 5 percent for Category A, or not more than 10 percent for Category B in accordance with Table 2. Table 2 Uniformity Values [Clauses 8.1.2.1 and l Itd)] Sl No Category Deviation of q from qx, max Coefficient of variation Cv (1) (2) (3) (4) i) A 5 5 ii) B 10 10 8.1.2.2 The co-efficient of variation (C) of the emission rate of the test sample shall not exceed 5 percent for Category A, or 10 percent for Category B. 8.1.3 Regulated Emitting Pipes Condition the emitting units in the test sample by operating them for one hour minimum at an emitting unit with inlet pressure equal to the pressure at the middle of the working pressure range. At the beginning of conditioning, the emitting units shall be operated three times at about Pmax and three times at about Pmin each operation to be maintained for at least three minutes. During the last 10 min of conditioning, the pressure shall be maintained at the midpoint of the range of regulation. Immediately after, and without altering the inlet pressure, test the emitting units according to 8.1.2 but at the midpoint of the range of regulation. 8.1.3.1 The emitting units shall comply with the requirements given in 8.1.2.1 and 8.1.2.2.
  • 21. 8.2Emission Rate of Emitting Unit as a Function of Inlet Pressure Number the emitting units tested according to 7.1, in ascending order according to the measured emission rate.(No. I shall be given to the emitting unit of lowest emission rateandNo.25 to the emitting units of highest emission rate). Select4 emitting units from the series obtained, No.3, 12, 13,23 and measure their change in emission rate as a function of the inlet pressure. Test each emitting unit in steps not greater than 50 kPa, from Pmin Up to 1.2Pmax Regulated emitting units shall be tested at three or more different pressures within the range of regulation, at rising and falling inlet pressure. The reading of the results shall be taken at least three minutes after arriving at the test pressure. If the inlet pressure exceeds the desired pressure by more than 10kPaduring its rise and fall, return to •Pmin and repeat the test. 8.2.1 Unregulated Emitting Pipe Calculate for each pressure value, the average emission rate q obtained by measuring the emission rate of the four emitting units at rising pressure. Plot the curve q as function of inlet pressure. 8.2.1.1 The curve of q shall conform to the curve presented in the publication of the manufacturer within an allowable deviation of not more than±5 percent for Category A and ±1O percent for Category B.
  • 22. 8.2.2 Regulated Emitting Pipes Calculate for each inlet pressure value , Pi the average emission rate q obtained by measuring the emission rate of the four emitting units at rising and falling pressure(the average of 8 emission rate measurement). 8.2.2.1 The value of q shall not deviate from the nominal emission rate by more than 5 percent for Category A or not more than 10 percent for Category B.
  • 23. 8.3 Dimensions 8.3.1 Wall Thickness of Emitting Pipe Measure the wall thickness of the emitting pipe at four points equally spaced on the periphery of the pipe. Repeat the test at two cross sections. In the event of a part the pipe wall being thicker by design(for example, flap in emitting pipe), such increase in thickness shall be disregarded. 8.3.1.1 The wall thickness of the emitting pipe, when measured at each of the four points, shall be within limits given in Table 1. 8.3.2 Inside Diameter of Emitting Pipe For measuring the inside diameter of emitting pipe, insert into the end of the pipe a specific taper gauge (with2°apexangle)or 'Go', 'No-Go’ gauge , first enter GO side of the gauge, it should go inside the tube without much force but at the same time it should not remain loose in the tube. For example a GO, NO-GO gauge sketch is given at Fig. 1 for 16 mm nominal diameter tube. Alternatively the outside diameter may be measured with pie tape or vernier caliper, from which two times the average thickness measured at the same point of pipe can be deducted to obtain the inside diameter.
  • 24. 8.3.2.1 The measured inside diameter shall be within the limits given in Table .
  • 25. 8.3.3 Flow Paths in Emitting Unit Measure in at least three emitting units, accurately to the nearest 0.02 mm and under no pressure, the smallest dimension of the flow path (this does not apply to dimension that varies with pressure). 8.3.3.1 The smallest measured flow path dimension shall not be smaller than the dimensions declared by the manufacturer. 8.3.4 Spacing of Emitter Units Measure three spacings of emitting units, accurately to the nearest 1.0 mm. 8.3.4.1 The spacing of the emitting units shall not deviate by more than 5 percent from the spacings declared by the manufacturer.
  • 26. 8.4 Resistance of Emitting Pipes to Hydrostatic Pressure 8.4.1 Resistance to Hydrostatic Pressure at Ambient Temperature Perform the test on a length of emitting pipe consisting of five unit emitting pipes joined by means of center fittings. Perform this test in two stages(see 8.4.1.1 and8.4.1.2). 8.4.1.1Connect the emitting pipe assembly to a source of water, by means of an inlet fitting, and close its outlet end. Fill the emitting pipe assembly with water and check that no air remains trapped in the pipe. Increase the water pressure gradually (10 s, Min) to the maximum working pressure multiplied by 1.8 and maintain the test pressure for 1 h. The emitting pipe assembly shall withstand the test pressure without showing signs of damage to the emitting pipe, the emitting units or the connecting fittings. The unit emitting pipes shall not pull apart, and no leakage shall occur at the inlet fitting. Leakages not exceeding the emission rate of one emitting unit are permissible at center fittings.
  • 27. 8.4.1.2 Reduce the test pressure to nominal pressure and maintain for at least 3 min. Measure the flow rate of each emitting unit. The flow rate of each emitting unit shall not deviate by more than 10 percent from its initially observed flow rate, as measured in 8.1. 8.4.2 Resistance to Hydrostatic Pressure at Elevated Temperature Perform the teston a length of emitting pipe consisting of 3 emitting-pipe units jointed by means of center fittings. Perform the test in two stages (see 8.4.2.1 and8.4.2.2). 8.4.2.1Connect the emitting-pipe assembly to a source of water, by means of an inlet fitting, and close its outlet end. Fill the emitting-pipe assembly with water and check that no air remains trapped in the pipe. Raise the water pressure gradually (10 s, Min) to maximum pressure and maintain the pressure for 48 h, while the emitting-pipe test assembly is immersed in water at 60:1: 2°C temperature. The emitting pipe shall withstand the test pressure without showing signs of damage.
  • 28. 8.4.2.2 Remove the test assembly from the water and maintain it for 30 min at ambient temperature. Apply a hydrostatic pressure Pn for at least 3 min at ambient temperature and measure the flow rate of each emitting unit. The flow rate of each emitting unit shall not deviate by more than 10 percent from its original flow rate, as measured in 8.1.
  • 29. 8.S Resistance to Tension at Elevated Temperature Perform the test on 5 unit emitting pipe at a temperature of 50:1: 2°C. NOTE- Mark on the unit emitting pipe two lines about 150 mm apart. Fasten one end of the emitting pipe in an air circulation oven maintained at 50 :t 2"C and apply a dead weight in accordance with Table 3. Maintain the pull for 15 min. then remove the pull and cool the unit emitting pipe to an ambient temperature. 8.5.1Emitting pipe shall withstand the test pull without breaking or tearing. The nominal flow rate in the test specimen shall not vary by more than 5 percent from the flow rate measured before testing according to 8.1, and the distance between the two marked lines shall not vary by more than 5 percent from the distance measured (see 8.5)
  • 30. 8.6 Resistance to Pull Out of Joints Between Fitting and Emitting This test shall be performed in accordance with IS 13479, but the test pull out load shall be according to Table3, applied for 1 hr or alternatively dead weight may be used for applying the test pull. The fitting shall not pull out from the emitting pipe.
  • 31. PRINCIPLE Checking of the ability of an assembled joint to resist pulling out when submitted to longitudinal tension. 3 APPARATUS Tensometer capable of holding the test specimen at a constant longitudinal stress . the design for jointing O pipe with ding 63 mm Alternatively, the calculated force may be applied to the specimen by means of weights, in which case the specimen shall be suspended on a frame with a suitable stirrup at the lower end of the specimen to hold the weights.
  • 32.
  • 33. • Resistance to ESCR : • 8.7.1 Acceptance Test (77°C & 1 Hr) • The test procedure shall conform to the procedure described in Annex D of IS 12786, except for the following: Condition the test specimen in an air circulating oven at 80:1: l°C for 1 h. • Then air cool and U bend the specimen and immerse in a constant temperature bath. Containing the reagent. • Percentage concentration = 10 percent of surface active agent • Test temperature = 77 ± 3°C • Test duration = 1 Hr • Reagent = Nonyl Phenoxy polyethyleneoxy ethanol ( Igepal CO-630) • Specimen size = 38 x 13 mm
  • 34. • 8.7.2 Type Test • The test procedure shall confirm to the procedure described in Annex D of IS 12786.except for the test temperature and test duration which shall be as specified below: • Percentage concentration = 10 percent of surface active agent • Test temperature = 77 ± 3°C • Test duration = 48 h • Reagent = Nonyl Phenoxy polyethyleneoxy ethanol ( Igepal CO-630) • Specimen size = 38 x 13 mm
  • 35. TEST METHOD D-2.1 Reagent An undiluted surface active agent of the type of nonylphenoxy poly ( ethyleneoxy ) ethanol [ Igepal CO-630 or Antarox CO-6301 may be used for reference purposes. This information is given for the convenience of users and does not constitute endorsement of the product kept in closed containers and used fresh for each test. D-2.2 Apparatus Forced air circulation oven, maintained at 50 ± 3°C, capable of re-establishing that temperature within five minutes after insertion of test pieces. D-2.3 Test Specimen Five sections of pipe, preferably from different coils, each of length about 20 times the diameter shall constitute the test piece.
  • 36. D-2.4 Procedure D-2.4.1 Bend each test piece sharply at two pieces, to form two U-bends, in two different planes perpendicular to each other (see fig -2 ).Each bend is worked to the limit , that is until both sides of the fold touch and lie parallel to each other, and then the bend is tightly secured to maintain that deformation throughout the test ( see Fig. 2 ). D-2.4.2 Coat each bend completely with the reagent by dipping and then place all the test pieces in the oven, taking care not to impose any additional stresses on them. -D-2.4.3 30 minutes after the temperature of the oven ( bath ) has returned to 50 f 3% take the test pieces out and release the stress and wipe the bends free from reagent. D-2.4.4 Inspect each bend thoroughly, with the unaided eye for any visible cracks ( generally originating at the two ends of the fold). D-2.5 Expression of Results Any bend which contains at least one visible crack (-excluding cracks induced by the object used to secure the bend ), is classified as failed. The total number of bends which fail shall be noted.
  • 37. 8.8 Determination of Emitting Unit Exponent (This Test Applies to Both Regulated and Unregulated Emitting Units) The relation between the emission rate. 𝑞. in 1/h and the inlet pressure in an emitting unit .P. in kilopascals, is given by the formula: 𝑞 = 𝑘 ⋅ 𝑝𝑚 m = 𝐥𝐨𝐠 𝒑𝒊 𝐥𝐨𝐠 𝒒ⅈ −𝟏 𝒏 𝜮 𝐥𝐨𝐠 𝒑𝒊 𝐥𝐨𝐠 𝒒ⅈ 𝐥𝐨𝐠 𝒑𝒊 𝟐−𝟏 𝒏 𝐥𝐨𝐠 𝒑𝒊 𝟐 where q =emission rate. in 1/h; k =constant; p = inlet pressure. in KPa; m =emitting unit exponent; i= 1.2.3.4.......... n; and n = number of pressure values used in 8.2.2.
  • 38. Using all the q and p values obtained in 8.2.2.calculate m from the above formula. The value of the emitting unit exponent m shall be less than0.5 for non-regulated emitting pipes and less than 0.2 for regulated emitting pipes.