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MEMBRANE TRANSFER TECHNOLOGY
Charles L. Kimbell President Keco R
& D, Incorporated Route 3, Box 141 Navasota, TX 77868 |
Bill Barnes Sales Coordinator Keco R
& D, Incorporated Route 3, Box 141 Navasota, TX 77868 |
KEYWORDS
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Membrane Transfer, Sample Permeation,
Permeation Transfer, Volatile Organic Carbon (VOC), Analyzer, VOC Remediation,
Emissions Reporting, Calibration |
ABSTRACT
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The use of a permeable membrane to monitor
volatile hydrocarbons including chlorinated hydrocarbons, alcohol and other
chemicals from low PPB to percent in a liquid or gas phase is practical. This
alternative to the sparger or purge and trap methods reduces maintenance for
GC's or other analyzers. |
INTRODUCTION
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Permeation has been around for many years
however, with the in depth research and development of the transfer unit,
Figure 1, there are many ways to use the unit that have not been recognized in
the past.
The main instrumentation use of the
transfer unit is to allow a hydrocarbon tainted liquid or gas to pass on one
side of a membrane and the hydrocarbon will permeate through the membrane where
a clean flowing gas will evaporate the hydrocarbons from the membrane surface
resulting in a clean dry sample suitable for an analyzer. Detectability is 1
PPB range to percent (1).
This eliminates use of heated injection
valves to vaporize a sample and also eliminate need for heat traced lines. The
clean, dry carrier gas prevents condensation in the flow lines.
Transfer units can operate for long periods
of time with a minimum of maintenance, as shown by results in petrochemical
plant testing.
Membrane tests are listed below, Table I.
Various GC analyzers were employed and flowrates were not adjusted for optimum
results. Detection limit was determined by multiplying the PPM weight by the
average noise divided by response at that PPM. |
TABLE I - RESPONSE USING MEMBRANE
TRANSFER SAMPLE INTO VARIOUS GC'S
TRACE
HYDRO- CARBON |
CONCEN- TRATION |
RES-
PONSE |
NOISE |
DETECT- ABLE PPB |
| Benzene in Water |
10 PPM |
672.0 |
0.3 |
4.4 PPB |
| Benzene in Water |
5 PPM |
229.0 |
0.5 |
10.9 PPB |
| Benzene in Water |
1 PPM |
170.0 |
5.0 |
29.4 PPB |
| Benzene in Water |
0.008 PPM |
600.0 |
100.0 |
13.3 PPB |
| Benzene Quinch Water |
5 PPM |
623.0 |
1.0 |
8.0 PPB |
| Trichloro Ethylene in Water |
1 PPM |
598.0 |
3.0 |
5.0 PPB |
| Tertiary Butyl Alcohol |
5 PPM |
265.0 |
0.5 |
9.4 PPB |
| Two techniques for dynamic calibration were
developed, one using the permeation tube and the other is the micro injection
system. The injector mechanically injects minute quantities of a pure substance
directly into flowing lines. This allows wide rangeability at PPM or PPB
levels. Flow rates ranging from 0.000020 ml/min to 0.003 ml/min were obtained
using an injection rate control. |
TABLE II - COMPARISON TEST SPARGER
VS TRANSFER UNIT
HYDRO- CARBON |
SPARGER
RESPONSE |
TRANSFER
UNIT RESPONSE |
| Ethylene-Ambient |
9.4 PPB |
6.3 PPB |
| Ethylene @ 55ºC |
12.2 PPB |
10.6 PPB |
| Propane-Ambient |
13.6 PPB |
15.7 PPB |
| Propane @ 55ºC |
11.25 PPB |
11.5 PPB |
| Methyl Chloride-Ambient |
23.1 PPB |
20.6 PPB |
| Methyl Chloride @
55ºC |
26.0 PPB |
19.5 PPB |
This set of data, Table II, was obtained in
an operating plant on actual cooling tower water lines using the same GC
readouts. Various types of membranes can be used. They can be used in water
streams to monitor for hydrocarbons; as an alternative to the sparger or the
purge and trap system. There is little maintenance to the transfer system which
is an essential component of the equipment making the method superior to the
older methods. Monitoring quinch ponds, cooling tower water and head
space in manholes or off plant water is all possible. The transfer unit can
also be used in liquid or head space above the liquid. Good results have been
obtained when analyzing for hydrocarbons being removed from plastic pellets by
steam or nitrogen.
Figure 2, is a chart recording showing calibration of a
Keco R & D, Inc., Model 204, benzene in cooling tower water analyzer. The
actual cooling tower water was scrubbed with a charcoal filter which provided a
zero benzene reading. A permeation tube designed to give 20 PPB by weight, read
as 19.5 PPBw was used. A second calibrator mechanically injects benzene into
clean water to the analyzer to provide 10 PPBw as shown on the right. The 7.7
PPBw reading correlates very well to the permeation tube calibration. This data
was obtained after shipping and installation, additional adjustments after the
original factory calibration were unnecessary.
The micro injection method of calibration is a new
development which allows over 100 to 1 ranging for linearity checking and
requires only a contact closure for automatic calibration. The sample is
prepared at the time of use eliminating degradation with time as can result
from bacterial action or absorption.
Figure 3, is a recording of cooling tower water with the
ethylene plant in normal operation. Both recordings show the GC reading of
benzene every four minutes shown as points on the long term graphs. Slight
fluctuations of benzene levels of 2.25 PPBw and 1.1 PPBw are shown over a 3 day
run. These fluctuations were caused by heat exchanger leaks. Disconnecting the
leaking heat exchanger corrected the problem as shown by the
recording. |
REFERENCES
| 1. |
Kimbell, Charles,
Barclay, Limuel, US Patent No. 5,448,922, Gas permeation system. |
| 2. |
John P. Survis,
Equivalency of Method Determination for Measurement of Volatile Organic
Compounds (VOC) by Semipermeable Membrane Transfer, Texas Natural Resources
Conservation Commission, letter May 10, 1996. |
| Home | |
Permeation Trans. Monitor | Volatile Hydro. Anal. | | Membrane Sample Trans. | Membrane Probe
Trans. | | Permeation Tube Calibrator |
Permeation Tubes | | Microliter
Fluid Calibrator | Sensor Calibration | |
Membrane Transfer Technology | TNRCC Letter |
Phone: 281-516-3950 Fax: 281-351-8925 E-Mail:
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© 1994-2001 Keco R.& D., Inc.
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