ASTM D5090-90(2001)
(Practice)Standard Practice for Standardizing Ultrafiltration Permeate Flow Performance Data
Standard Practice for Standardizing Ultrafiltration Permeate Flow Performance Data
SCOPE
1.1 This practice covers the standardization of permeate flow for ultrafiltration (UF) systems.
1.2 This practice is applicable to natural waters including brackish waters, seawaters, and ultrapure waters including those used in power generation and microelectronics and pharmaceuticals production. It is not necessarily applicable to waste waters.
1.3 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
Relations
Standards Content (Sample)
NOTICE: This standard has either been superseded and replaced by a new version or withdrawn.
Contact ASTM International (www.astm.org) for the latest information
Designation: D 5090 – 90 (Reapproved 2001)
Standard Practice for
Standardizing Ultrafiltration Permeate Flow Performance
Data
This standard is issued under the fixed designation D 5090; 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.
1. Scope 3.2.6 recovery or conversion—the ratio of permeate flow
rate to total feed flow rate, expressed as a percent.
1.1 This practice covers the standardization of permeate
3.2.7 stage—a device or group of devices, several of which
flow for ultrafiltration (UF) systems.
may be included in a system, which share common manifolds
1.2 This practice is applicable to natural waters including
on the feed, concentrate and permeate stream plumbing. The
brackish waters, seawaters, and ultrapure waters including
concentrate from one stage becomes the feed to the following
those used in power generation and microelectronics and
stage.
pharmaceuticals production. It is not necessarily applicable to
3.2.8 ultrafiltration device—a single housing (vessel), com-
waste waters.
prising or containing an ultrafiltration element or multiple
1.3 This standard does not purport to address all of the
elements and supporting materials.
safety concerns, if any, associated with its use. It is the
responsibility of the user of this standard to establish appro-
4. Summary of Practice
priate safety and health practices and determine the applica-
4.1 This practice consists of calculating the permeate flow
bility of regulatory limitations prior to use.
of UF systems at a standard set of conditions using data
2. Referenced Documents obtained at actual operating conditions.
2.1 ASTM Standards:
5. Significance and Use
D 1129 Terminology Relating to Water
5.1 During the operation of a UF system, conditions includ-
3. Terminology ing pressure and temperature, can vary, causing permeate flow
to change (see Note 1). To effectively evaluate system perfor-
3.1 Definitions—For definitions of terms used in this prac-
mance, it is necessary to compare permeate flow data at the
tice, refer to Terminology D 1129.
same conditions. Since data may not always be obtained at the
3.2 Definitions of Terms Specific to This Standard:
sameconditions,itisnecessarytoconverttheUFdataobtained
3.2.1 concentrate, reject, or brine—that portion of feed
at actual conditions to a set of constant conditions, thereby
which does not pass through the membrane.
standardizing the data. The user of this practice determines the
3.2.2 device pressure drop (DP)—the difference between
standard conditions. This practice gives the procedure to
the feed pressure and the concentrate pressure.
standardize UF data on pure water only.
3.2.3 feed—the fluid that enters the device.
3.2.4 permeate—that portion of the feed which passes
NOTE 1—Feed concentration, crossflow velocity, and both device and
through the membrane.
total system recovery will also influence permeate rate, especially when
operating on other than pure water. This practice does not address those
3.2.5 permeate flow rate—the quantity of permeate pro-
system conditions.
duced per unit time.
5.2 This practice can be used for systems which contain
spiral-wound, tubular, plate and frame, and hollow fiber
This practice is under the jurisdiction of ASTM Committee D19 on Water and
devices.
is the direct responsibility of Subcommittee D19.08 on Membranes and Ion
5.3 This practice can be used for a single-element or a
Exchange Materials.
multi-element system. However, if the UF system is staged,
Current edition approved June 29, 1990. Published February 1991.
Annual Book of ASTM Standards, Vol 11.01. standardize the permeate flow and salt passage for each stage
Copyright © ASTM International, 100 Barr Harbor Drive, PO
...
Questions, Comments and Discussion
Ask us and Technical Secretary will try to provide an answer. You can facilitate discussion about the standard in here.