ASTM C1051-85(1994)e1
(Specification)Standard Specification for Sodium (Na) as a Coolant for Liquid Metal-Cooled Reactors (Withdrawn 2000)
Standard Specification for Sodium (Na) as a Coolant for Liquid Metal-Cooled Reactors (Withdrawn 2000)
SCOPE
1.1 This specification is for sodium intended for use in liquid metal-cooled reactors and for related, non-reactor test and experimental systems.
1.2 The values stated in SI units are to be regarded as the standard.
1.3 The following precautionary caveat pertains only to Section 7 of this specification: This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use.
General Information
Standards Content (Sample)
e1
Designation: C 1051 – 85 (Reapproved 1994)
AMERICAN SOCIETY FOR TESTING AND MATERIALS
100 Barr Harbor Dr., West Conshohocken, PA 19428
Reprinted from the Annual Book of ASTM Standards. Copyright ASTM
Standard Specification for
Sodium (Na) as a Coolant for Liquid Metal-Cooled Reactors
This standard is issued under the fixed designation C 1051; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
e NOTE—Sections 9 and 10 were renumbered and keywords were added editorially in August 1994.
1. Scope have become contaminated with sodium not meeting the
chemical purity specification for use in Class I or Class II
1.1 This specification is for sodium intended for use in
systems.
liquid metal-cooled reactors and for related, non-reactor test
3.1.4 lot—the quantity of sodium contained in a filled tank
and experimental systems.
car of the type approved for sodium shipment under
1.2 The values stated in SI units are to be regarded as the
49CFR173.
standard.
1.3 The following precautionary caveat pertains only to
4. Classification
Section 7 of this specification: This standard does not purport
4.1 Class I System—All sodium systems associated with a
to address all of the safety concerns, if any, associated with its
liquid metal cooled reactor.
use. It is the responsibility of the user of this standard to
4.2 Class II System—Non-reactor related test and experi-
establish appropriate safety and health practices and deter-
mental sodium systems.
mine the applicability of regulatory limitations prior to use.
5. Ordering Information
2. Referenced Documents
5.1 The buyer shall furnish the seller with the following
2.1 ASTM Standards:
information in a purchasing agreement:
C 997 Test Methods for Chemical and Instrumental Analy-
5.1.1 Quantity of sodium to be delivered and whether the
sis of Nuclear-Grade Sodium and Cover Gas
chemical requirements for Class I or Class II systems are
G 68 Practice for Liquid Sodium Corrosion Testing of
applicable.
Metals and Alloys
5.1.2 ASTM designation and year of issue of this standard
2.2 U.S. Government Document:
and all other applicable standards.
Title 49, Code of Federal Regulations, Hazardous Materials
5.1.3 Name of buyer, delivery site, and delivery date.
Regulations of the Department of Transportation, Parts
5.1.4 Type of shipping container and type of cover gas to be
171–179
used.
5.1.5 Method of shipment.
3. Terminolgy
5.1.6 Minimum cleaning and inspection plan requirements
3.1 Descriptions of Terms Specific to This Standard:
for shipping containers and sodium transfer piping.
3.1.1 batch—the quantity of sodium contained in drums
5.1.7 Any specific sampling, testing, certification, cleanli-
filled from a single sodium source produced under a specific
ness, packaging, shipping, or quality verification plans or
purchasing agreement; the drums to be of the type approved for
requirements that may have been mutually agreed to by the
sodium shipment.
buyer and seller.
3.1.2 filter—a flow through device containing a metal
6. Filtering and Chemical Composition
screen or frit constructed of a suitable material, such as Type
304 or Type 316 stainless steel, which is used to retain 6.1 Filtering Requirements—Sodium intended for use in
particulate material that may be present in liquid sodium.
Class I and Class II systems shall be melted and filtered at a
3.1.3 line volume—the internal volume enclosed by piping temperature not greater than 150°C (300°F) through a filter of
surfaces of a sodium delivery system which historically could
28-μm porosity. This filtration is to occur prior to any sampling
of the sodium for chemical analysis and before loading the
sodium into any shipping container.
This specification is under the jurisdiction of ASTM Committee C-26 on
6.2 The chemical requirements of sodium for use in Class I
Nuclear Fuel Cycle and is the direct responsibility of Subcommittee C26.02 on Fuel
or Class II system shall be as follows:
and Fertile Material Specifications.
Current edition approved Nov. 29, 1985. Published January 1986.
6.2.1 Class I—The total sodium plus potassium content of
Annual Book of ASTM Standards, Vol 12.01.
this material shall be no less than 99.90 weight %. The
Annual Book of ASTM Standards, Vol 03.02.
impurity content of this material shall not exceed the limits
Available from Superintendent of Documents, U.S. Government Printing
Office, Washington, DC 20402. specified in Table 1.
C 1051
TABLE 1 Impurity Content of Sodium for Class I System Use
or batch (drums). Sampling, weighing of the sample, and
Allowable Concentration Limit, handling shall be done under conditions which assure that the
Element
μg/g
sample does not become contaminated and is representative of
Boron 5
the lot or batch. A sampling plan and the method for taking the
Calcium 10
samples shall be mutually agreed upon between the buyer and
Carbon 30
the seller. Each sample shall be tagged to show the date,
Chlorine 30
Lithium 1
purchase order number, lot or batch number, and sample
Potassium 500
sequence under the sampling plan.
Sulfur 10
8.2 Filter requirements shall be part of the sampling plan
Uranium 0.01
Total other impurities 900
mutually agreed upon between the buyer and the seller.
9. Container Preparation
6.2.2 Class II—The total sodium plus potassium content of
this material shall be no less than 99.90 weight %. This 9.1 Cleanliness—The seller shall furnish a detailed clean-
material shall have an individual element and total impurity ing, inspection, and filtering plan and procedures for the
content limit of (a) no more than 10 μg/gram of calcium, (b)no buyer’s approval prior to filling any shipping containers with
more than 1000 μg/gram of potassium, and (c) no more than sodium unless otherwise specified in the purchasing agree-
990 μg/gram of the total of other impurities. ment. No filling of sodium shipping containers shall be started
until all requirements have been approved by the buyer in
7. Hazards and Safety Precautions
writing.
7.1 Sodium is a chemically active metal and, depending on
9.2 Tank Cars—Tank cars used to transport Class I and
temperature, can react at rates varying from slow to violent
Class II sodium shall meet the following cleanliness require-
with oxidizers (such as, oxygen and water), compounds with
ments unless otherwise specified in the purchasing agreement:
labile hydrogen (such as, acids and alcohols) and with certain
9.2.1 The interior surfaces of the tank car shall be clean to
organics (such as, halogenated hydrocarbons). Contact be-
the extent that no contamination will be visible on any surface.
tween solid or liquid sodium and water or water vapor must be
Thin adherent films of rust, defined as superficially corroded
avoided as sodium hydroxide and hydrogen are formed and the
areas of red, brown, or black discolorations are acceptable
reaction can proceed at a rate which liberates sufficient heat to
provided that no more than 1 % of the total inside surface
...
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