SIST EN ISO 13503-5:2007

SLOVENSKI STANDARD
SIST EN ISO 13503-5:2007
01-januar-2007
Industrija za predelavo nafte in zemeljskega plina - Tekočine in materiali za
zaključna dela - 5. del: Postopki za merjenje dolgoročne prevodnosti podpornih
materialov (ISO 13503-5:2006)
Petroleum and natural gas industries - Completion fluids and materials - Part 5:
Procedures for measuring the long-term conductivity of proppants (ISO 13503-5:2006)
Erdöl- und Erdgasindustrie - Komplettierungsflüssigkeiten und Materialien - Teil 5:
Verfahren zur Messung der Langzeitleitfähigkeit von Stützmaterialien (ISO 13503-
5:2006)
Industries du pétrole et du gaz naturel - Fluides de complétion et matériaux - Partie 5:
Modes opératoires pour mesurer la conductivité a long terme des agents de
soutenement (ISO 13503-5:2006)
Ta slovenski standard je istoveten z: EN ISO 13503-5:2006
ICS:
75.100 Maziva Lubricants, industrial oils and
related products
75.180.30 Oprema za merjenje Volumetric equipment and
prostornine in merjenje measurements
SIST EN ISO 13503-5:2007 en
2003-01.Slovenski inštitut za standardizacijo. Razmnoževanje celote ali delov tega standarda ni dovoljeno.

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SIST EN ISO 13503-5:2007

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SIST EN ISO 13503-5:2007
EUROPEAN STANDARD
EN ISO 13503-5
NORME EUROPÉENNE
EUROPÄISCHE NORM
July 2006
ICS 75.100

English Version
Petroleum and natural gas industries - Completion fluids and
materials - Part 5: Procedures for measuring the long-term
conductivity of proppants (ISO 13503-5:2006)
Industries du pétrole et du gaz naturel - Fluides de Erdöl- und Erdgasindustrie - Komplettierungsflüssigkeiten
complétion et matériaux - Partie 5: Modes opératoires pour und Materialien - Teil 5: Verfahren zur Messung der
mesurer la conductivité à long terme des agents de Langzeitleitfähigkeit von Stützmaterialien (ISO 13503-
soutènement (ISO 13503-5:2006) 5:2006)
This European Standard was approved by CEN on 24 May 2006.
CEN members are bound to comply with the CEN/CENELEC Internal Regulations which stipulate the conditions for giving this European
Standard the status of a national standard without any alteration. Up-to-date lists and bibliographical references concerning such national
standards may be obtained on application to the Central Secretariat or to any CEN member.
This European Standard exists in three official versions (English, French, German). A version in any other language made by translation
under the responsibility of a CEN member into its own language and notified to the Central Secretariat has the same status as the official
versions.
CEN members are the national standards bodies of Austria, Belgium, Cyprus, Czech Republic, Denmark, Estonia, Finland, France,
Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania,
Slovakia, Slovenia, Spain, Sweden, Switzerland and United Kingdom.
EUROPEAN COMMITTEE FOR STANDARDIZATION
COMITÉ EUROPÉEN DE NORMALISATION
EUROPÄISCHES KOMITEE FÜR NORMUNG
Management Centre: rue de Stassart, 36  B-1050 Brussels
© 2006 CEN All rights of exploitation in any form and by any means reserved Ref. No. EN ISO 13503-5:2006: E
worldwide for CEN national Members.

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SIST EN ISO 13503-5:2007

EN ISO 13503-5:2006 (E)





Foreword


This document (EN ISO 13503-5:2006) has been prepared by Technical Committee ISO/TC 67
"Materials, equipment and offshore structures for petroleum and natural gas industries" in
collaboration with Technical Committee CEN/TC 12 "Materials, equipment and offshore
structures for petroleum, petrochemical and natural gas industries", the secretariat of which is
held by AFNOR.

This European Standard shall be given the status of a national standard, either by publication of
an identical text or by endorsement, at the latest by January 2007, and conflicting national
standards shall be withdrawn at the latest by January 2007.

According to the CEN/CENELEC Internal Regulations, the national standards organizations of
the following countries are bound to implement this European Standard: Austria, Belgium,
Cyprus, Czech Republic, Denmark, Estonia, Finland, France, Germany, Greece, Hungary,
Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland,
Portugal, Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland and United Kingdom.


Endorsement notice

The text of ISO 13503-5:2006 has been approved by CEN as EN ISO 13503-5:2006 without any
modifications.

2

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SIST EN ISO 13503-5:2007


INTERNATIONAL ISO
STANDARD 13503-5
First edition
2006-07-01


Petroleum and natural gas industries —
Completion fluids and materials —
Part 5:
Procedures for measuring the long-term
conductivity of proppants
Industries du pétrole et du gaz naturel — Fluides de complétion et
matériaux —
Partie 5: Modes opératoires pour mesurer la conductivité à long terme
des agents de soutènement




Reference number
ISO 13503-5:2006(E)
©
ISO 2006

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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
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©  ISO 2006
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ii © ISO 2006 – All rights reserved

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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
Contents Page
Foreword. iv
Introduction . v
1 Scope . 1
2 Normative reference . 1
3 Terms and definitions. 1
4 Abbreviations . 2
5 Procedures for evaluating long-term proppant pack conductivity . 2
5.1 Objective. 2
5.2 Discussion. 2
6 Reagents and materials . 3
6.1 Test fluid . 3
6.2 Sandstone. 3
7 Long-term conductivity test apparatus . 3
7.1 Test unit . 3
7.2 Hydraulic load frame . 3
7.3 Pack width measurement device(s). 3
7.4 Test fluid drive system. 3
7.5 Differential pressure transducers . 4
7.6 Back-pressure regulators . 4
7.7 Balance . 4
7.8 Oxygen removal. 4
7.9 Temperature control. 4
7.10 Silica saturation and monitoring. 5
8 Equipment calibration . 5
8.1 Pressure indicators and flow rates. 5
8.2 Zero pack width measurement . 5
8.3 Determination of cell width. 6
8.4 Hydraulic load frame . 6
9 Leak tests . 6
9.1 Hydraulic load frame . 6
9.2 Test fluid system. 6
10 Procedure for loading the cells . 6
10.1 Preparation of the test unit . 6
10.2 Cell setup. 7
11 Loading cell(s) in the press . 9
12 Acquiring data. 9
13 Calculation of permeability and conductivity . 10
14 Data reporting . 11
Annex A (informative) Conversion factors . 12
Annex B (normative) Silica-saturation vessel setup . 13
Annex C (informative) Figures .15
Bibliography . 24

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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
Foreword
ISO (the International Organization for Standardization) is a worldwide federation of national standards bodies
(ISO member bodies). The work of preparing International Standards is normally carried out through ISO
technical committees. Each member body interested in a subject for which a technical committee has been
established has the right to be represented on that committee. International organizations, governmental and
non-governmental, in liaison with ISO, also take part in the work. ISO collaborates closely with the
International Electrotechnical Commission (IEC) on all matters of electrotechnical standardization.
International Standards are drafted in accordance with the rules given in the ISO/IEC Directives, Part 2.
The main task of technical committees is to prepare International Standards. Draft International Standards
adopted by the technical committees are circulated to the member bodies for voting. Publication as an
International Standard requires approval by at least 75 % of the member bodies casting a vote.
Attention is drawn to the possibility that some of the elements of this document may be the subject of patent
rights. ISO shall not be held responsible for identifying any or all such patent rights.
ISO 13503-5 was prepared by Technical Committee ISO/TC 67, Materials. equipment and offshore structures
for petroleum, petrochemical and natural gas industries, Subcommittee SC 3, Drilling and completion fluids,
and well cements.
ISO 13503 consists of the following parts, under the general title Petroleum and natural gas industries —
Completion fluids and materials:
⎯ Part 1: Measurement of viscous properties of completion fluids
⎯ Part 2: Measurement of properties of proppants used in hydraulic fracturing and gravel-packing
operations
⎯ Part 3: Testing of heavy brines
⎯ Part 4: Procedure for measuring stimulation and gravelpack fluid leakoff under static conditions
⎯ Part 5: Procedures for measuring the long-term conductivity of proppants
iv © ISO 2006 – All rights reserved

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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
Introduction
[1]
This part of ISO 13503 is largely based on API RP 61 . Informative references are also included in the
Biblography, References [2] to [15].
The tests and test apparatus herein have been developed to establish standard procedures and conditions for
use in evaluating the long-term conductivity of various hydraulic fracture proppant materials under laboratory
conditions. This procedure enables users to compare the conductivity characteristics under the specifically
described test conditions. The test results can aid users in comparing proppant materials for use in hydraulic
fracturing operations.
The procedures presented in this publication are not intended to inhibit the development of new technology,
materials improvements, or improved operational procedures. Qualified engineering analysis and sound
judgment is required for their application to fit a specific situation.
This part of ISO 13503 may be used by anyone desiring to do so. Every effort has been made by ISO and API
to ensure the accuracy and reliability of the data contained in it. However, ISO and API make no
representation, warranty, or guarantee in connection with this part of ISO 13503, and hereby expressly
disclaim any liability or responsibility for loss or damage resulting from its use or for the violation of any federal,
state, or municipal regulation with which this part of ISO may conflict.
In this part of ISO 13503, where practical, U.S. customary units are included in parentheses for information.

© ISO 2006 – All rights reserved v

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SIST EN ISO 13503-5:2007

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SIST EN ISO 13503-5:2007
INTERNATIONAL STANDARD ISO 13503-5:2006(E)

Petroleum and natural gas industries — Completion fluids and
materials —
Part 5:
Procedures for measuring the long-term conductivity of
proppants
CAUTION — The testing procedures in this part of ISO 13503 are not designed to provide absolute
values of proppant conductivity under downhole reservoir conditions. Long-term test data have
shown that time, elevated temperatures, fracturing fluid residues, cyclic stress loading, embedment,
formation fines and other factors further reduce fracture proppant pack conductivity. Also, this
reference test is designed to measure only the frictional energy losses corresponding to laminar flow
within a pack. It is recognized that fluid velocity within an actual fracture can be significantly higher
than in these laboratory tests, and can be dominated by inertial effects.
1 Scope
This part of ISO 13503 provides standard testing procedures for evaluating proppants used in hydraulic
fracturing and gravel-packing operations.
NOTE The “proppants” mentioned henceforth in this part of ISO 13503 refer to sand, ceramic media, resin-coated
proppants, gravel packing media, and other materials used for hydraulic fracturing and gravel-packing operations.
The objective of this part of ISO 13503 is to provide consistent methodology for testing performed on
hydraulic-fracturing and/or gravel-packing proppants. It is not intended for use in obtaining absolute values of
proppant pack conductivities under downhole reservoir conditions.
2 Normative reference
The following referenced document is indispensable for the application of this document. For dated references,
only the edition cited applies. For undated references, the latest edition of the referenced standard (including
any amendments) applies.
ISO 3506-1, Mechanical properties of corrosion-resistant stainless-steel fasteners — Part 1: Bolts, screws and
studs
3 Terms and definitions
3.1
conductivity
width of the fracture multiplied by the permeability of the proppant pack
3.2
laminar flow
type of streamlined flow for single-phase fluids in which the fluid moves in parallel layers, or laminae, such that
the layers flow smoothly over each other with instabilities being dampened by the viscosity
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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
3.3
Ohio sandstone
fine-grained sandstone found in the United States from the Scioto Formation in southern Ohio
3.4
permeability
a measure of the ability of media to transmit fluid through pore spaces
4 Abbreviations
API American Petroleum Institute
ASTM American Society for Testing and Materials
RTV Room temperature vulcanizing
ANSI American National Standards Institute
PID Proportional-integral device
5 Procedures for evaluating long-term proppant pack conductivity
5.1 Objective
The objective is to establish a standard test procedure, using a standard apparatus, under standard test
conditions to evaluate the long-term conductivity of proppants under laboratory conditions. This procedure is
used to evaluate the conductivity of proppants under laboratory conditions but is not intended for use in
obtaining absolute values of proppant pack conductivities under downhole reservoir conditions. The effects of
fines, formation hardness, resident fluids, time, and/or other factors are beyond the scope of this procedure.
5.2 Discussion
In this part of ISO 13503 procedure, a closure stress is applied across a test unit for 50 h ± 2 h to allow the
proppant sample bed to reach a semi-steady state condition. As the fluid is forced through the proppant bed,
the proppant pack width, differential pressure, temperature and flow rates are measured at each stress level.
Proppant pack permeability and conductivity are calculated.
Multiple flow rates are used to verify the performance of the transducers, and to determine darcy flow regime
at each stress; an average of the data at these flow rates is reported. A minimum pressure drop of 0,01 kPa
(0,002 0 psi) is recommended; otherwise, flow rates shall be increased. At stipulated flow rates and
temperature conditions, no appreciable non-darcy flow or inertial effects are encountered. After completing the
rates at a closure stress level in all cells, the closure stress is increased to a new level; 50 h ± 2 h is allowed
for the proppant bed to reach a semi-steady state condition, and multiple flow rates in all cells are introduced
to gather data required to determine proppant pack conductivity at this stress level. The procedure is repeated
until all desired closure stresses and flow rates have been evaluated. To achieve accurate conductivity
measurements, it is essential that single-phase flow occurs.
Test condition parameters, such as test fluid, temperature, loading, sandstone and time, at each stress shall
be reported along with long-term conductivity and permeability data. Other conditions can be used to evaluate
different characteristics of proppants and, therefore, can be expected to produce differing results.
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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
6 Reagents and materials
6.1 Test fluid
The test fluid is 2 % by mass potassium chloride (KCl) in a deionized or distilled-water solution filtered to at
least 7 µm. The potassium chloride shall be at least 99,0 % by mass pure.
6.2 Sandstone
Ohio sandstone cores should have dimensions of 17,70 cm to 17,78 cm (6,96 in to 7,00 in) in length, 3,71 cm
to 3,81 cm (1,46 in to 1,50 in) wide, and a minimum of 0,9 cm (0,35 in) thick. The ends of the sandstone cores
shall be rounded to fit into the test unit (see 7.1). Parallel thickness shall be maintained within ± 0,008 cm
(± 0,003 in).
7 Long-term conductivity test apparatus
7.1 Test unit
2 2
The test unit shall be a linear flow design with a 64,5 cm (10 in ) proppant and bed area. Figure C.1
illustrates the details of the test unit and an example of how cells can be stacked. The pistons and test
1)
chamber(s) shall be constructed of 316 stainless steel (e.g. ISO 3506-1, Grade A4), Monel or Hastalloy
material. Filters for the test unit may be constructed using Monel wire cloth with an opening of 150 µm or
equivalent (100 US mesh). Nominal particle retention sizes are greater than 114 µm.
7.2 Hydraulic load frame
The hydraulic load frame shall have sufficient capacity to develop 667 kN (150 000 lbf). To ensure uniform
stress distribution, the platens shall be parallel to each other. It is recommended that the hydraulic load frame
be of a four-post design that minimizes warping that can be transmitted to the test cell. Each post should have
a minimum diameter of 6,35 cm (2,5 in).
The hydraulic pressurization source shall be capable of holding any desired closure stress [± 1,0 % or
345 kPa (50 psi), whichever is greater] for 50 h. The hydraulic load frame shall be capable of loading rate
2 2
changes of 4 448 N/min (1 000 lbf/min) or 690 kPa/min (100 psi/min) on a 64,5 cm (10 in ) cell. A calibrated
electronic load cell shall be used to calibrate the stress between the hydraulic ram and the opposing platen of
the load frame.
7.3 Pack width measurement device(s)
Pack width measurements shall be made at each end of the test unit. A measuring device capable of
measuring to 0,002 5 cm (0,001 in) accuracy or better shall be used. Figure C.4 shows an example of width
slats allowing for the measurement of pack widths.
7.4 Test fluid drive system
Some constant-flow-rate pumps (e.g. chromatographic pumps) have been found satisfactory for this
application. Pulsation dampening can be necessary and can be accomplished by use of a piston, bladder
accumulator or other effective means. Pressure fluctuations during differential pressure and flow rate
measurements (for conductivity calculations) shall be maintained at less than 1,0 %. Each laboratory shall
determine the best technique for pulsation dampening. Large pressure spikes can be indicative of pump
problems or trapped gas in the flow system and shall be corrected before recording data.

1) Monel and Hastalloy are examples of suitable products available commercially. This information is given for the
convenience of users of this part of ISO 13503 and does not constitute an endorsement by ISO of this product.
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SIST EN ISO 13503-5:2007
ISO 13503-5:2006(E)
7.5 Differential pressure transducers
Differential pressure transducers with a range of 0 kPa to 7 kPa (0 psi to 1,0 psi) are satisfactory. The
transducer shall be capable of measuring the differential pressure to ± 0,1 % of full scale.
7.6 Back-pressure regulators
The back-pressure regulator shall be capable of maintaining a pressure of 2,07 MPa to 3,45 MPa (300 psi to
500 psi). The stress applied to the cells shall take into account the back-pressure. For example, if the back-
pressure is 3,45 MPa (500 psi), then the applied stress shall be 3,45 MPa (500 psi) greater to take into
account the pressure exerted outward from the pistons.
7.7 Balance
The balance shall be capable of accommodating a minimum capacity of 100 g with a precision greater than
0,01 g.
7.8 Oxygen removal
The conductivity test fluid shall have the oxygen content reduced to simulate reservoir fluids and to minimize
corrosion of test equipment. De-oxygenation can be accomplished with a two-reservoir system for the fluid.
The first reservoir holds fluid for oxygen removal. This is connected to nitrogen gas that is bubbled through the
fluid at low pressure below 103 kPa (15 psi) and at low rate. The nitrogen supply is first passed through an
2)
oxygen/moisture trap such as Agilent Model OT3-4 that has an efficiency to remove oxygen to less than
15 µg/l. An equivalent system can be made; this system allows nitrogen to pass through heated copper
shavings at 370 °C (698 °F), where the copper reacts with the trace amounts of oxygen in the system forming
3)
copper oxide. An indicating trap, such as the oxygen trap by Chrom Tech, Inc. part # 10T-4-HP , after the
oxygen-removal process allows for visual confirmation that oxygen has been removed. When the visual
indicating trap is oxygen-saturated, both traps shall be replaced to maintain the efficiency of oxygen removal.
The second reservoir holds the oxygen-free fluid; this is the supply reservoir for the pumping system.
All fluids in each reservoir are held in sealed, inert-gas pressurized containers to eliminate oxygen
contamination from the air.
7.9 Temperature control
The test cell and proppant pack shall be maintained at the desired temperature ± 1 °C (± 3 °F). The
temperature for the test conditions is measured in the temperature port of the conductivity cell (Figure C.1).
This temperature is used to determine the fluid viscosity from Table C.1. The thermocouple assembly is split
into a temperature-control device and a data-acquisition system or equivalent. The temperature control
devices shall be programmable PID controllers and capable of self-tuning for different temperature conditions
and flow rates.
A temperature of 121 °C (250 °F) is employed in the test for ceramics and resin-coated proppants and 66 °C
(150 °F) for naturally occurring sands. The temperature for the silica-saturation vessel (see Annex B) should
be 11 °C (20 °F) above testing temperature of 66 °C (150 °F) for naturally occurring sands. Sand 20 °C
(35 °F) above 121 °C (250 °F) is used for resin-coated and ceramic proppants to ensure that the fluid is
saturated with silica prior to reaching the cell. Care shall be taken to ensure that the fluid arriving to the cell is
at the appropriate temperature. Tests using other fluids or temperatures can be of value in evaluating
proppant pack conductivity.

2) Agilent Model OT3-4 is an example of a suitable product available commercially. This information is given for the
convenience of users of this part of ISO 13503 and does not constitute an endorsement by ISO of this product.
3) Chrom Tech, Inc. part # 10T-4-HP is an example of a suitable product available commercially. This information is
given for the convenience of users of this part of ISO 13503 and does not constitute an endorsement by ISO of this
product.
4 © ISO 2006 – All rights reserved

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SIST EN ISO 13503-5:2007
ISO 13503-5:200
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