0 ratings0% found this document useful (0 votes) 189 views27 pagesPda TR9-1988
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content,
claim it here.
Available Formats
Download as PDF or read online on Scribd
“re
abekt3)
Butea
Nee
NaS
‘echnical Report No. 9
Review of Commercially
Available Particulate
Measurement Systems
Journal of Parenteral
Science and Technology
eens tayReview of Commercially Available Particulate Measurement Systems
Preface
In 1986, the Parenteral Drug Association Research Committee solicited proposals
for a grant concerning an engineering related analysis of existing liquid-borne particle
measuring equipment, Mr. Julius Knapp (R&D Engineering) and Dr. Patrick DeLuca
(University of Kentucky) were co-recipients of the grant.
The PDA has elected to publish the completed report of Mr. Knapp and Dr. DeLuca
to serve as a possible basis for further discussion among the parenteral technology
industry, and to perhaps provide the Research Committee with future constructive
research project ideas related to particulate technology.
‘The contents of Mr. Knapp’s and Dr. DeLuca’s report contains technical statements |
and conclusions attained by the authors independent of the PDA Association and are
not intended to reflect technical positions or interests of the PDA Research Committe, |
Board of Directors, and/or the Association at large.
Michael S. Korezynski, Ph.D.
Chairman, PDA Research Committee
August 1987
Vol. 42, Supplement 1988 83Contents
Part I—Instrumentation
1. Introduetion ss
HI, Common Factors... : Ss
III, Optical Systems es . $7
A. Filmy Materials feceeeee S8
B. Refractive Index Effects : $8
C. Conclusions : coo S8
IV. Resistance Modulation Systems (Coulter, etc.) BenBe ap a5H0a50008 so
A. Shape Sensitivity ceoset teste s9
B. Filmy and Porous Materials : S10
C. Sample Handling : S10
D. Conclusions Sil
V. Present Detection Systems er eos SH
‘A. Comparison poebesnesnsososon6s sul
B. Conclusions siz
VI. Recent FDA Test Results eects see SIZ
VII. Recommended Actions : s13
A. Stop Gap S13
B, Near Term ceo SB
VITI, Longer Term Actions : cece si3
IX. Future Perspectives : sects S13
A. All Systems o : cecseeeee si3
B, Coulter System . : see SI
C. Optical Detection Systems : : see SB
X. Notes cists . : . Sid
Appendix I: Commercially Available Particulate Measurement Systems for Parenteral Use
Descriptions and Comments si4
Appendix Il: Coincidence Errors in Particulate Counters... . : sis
Appendix III: “Ideal” Particulate Measurement S) Si8
Part II—A Selected Annotated Bibliography on Particulate Matter
1. Particle Counting (Size Analysis) . 7 : S19
A. General ppsossupsbeosoueGba cece 819
B. Large Volume Solutions cee : ceveeee $20
€. Small Volume Solutions ceo = S20
D. Injectable Powders seeseeeeee S21
E, Release from Bags sects SD
F, Release from Syringes and Needles teeceessseenste SB
G. Release from Administration Sets Beco S22
H. Release from Containers... Sospaceosse 2
1, Factors Influencing Particulate Matter ceo 82
1, Methods Evaluation : ere $23
A. General 5 eeerrenen sees SB
B. Microscope een : ves $B
C. Resistance : cece S24
D. Light Blockage .. - : S25
E. Light Scattering : : : : S25
F, Others... = : $25
IIL Identification cies S26
IV. Clinical Effects : pense seHo0EEo S26
V. Official Limits (Standards)... . -. 826
VI. Visual Inspection . cee S27
VII. Unpublished Articles and Letters .........+ aon see SH
sa ‘Journal of Parenteral Science & TechnologyPart |—Instrumentation
JULIUS Z, KNAPP* and PATRICK P. DeLUCAT
* Research & Development Associates, Inc, Somerset, New Jersey. ' University of Kentucky, College of Pharmacy, Lexington,
Kentucky
ABSTRACT: An objective review of the parenteral particulate measurement literature and the instrumenta-
tion now marketed for the analysis of particulates in parenteral solutions has been completed. This review
was undertaken with the goal of resolving the confusion of measurements presently surrounding the determi-
nation of particulate contamination in parenteral preparations and to provide an informed basis for anaction
plan. The conclusion reached is that the present lack of agreement in these measurements is the result of a
comtbination of factors. Most of these factors are traced to instrument limitations and a combination of
shortcomings in both sample handling technique and methodology. The review is in two parts: Part 1,
“Instrumentation” in which measurement techniques and problems are evaluated and Part II, “A Selected
Annotated Bibliography on Particulate Matter.” The Bibliography provides an overview of particulates in
parenteral solutions emphasizing instrument evaluations and comparisons.
|. Introduction
An objective review of the parenteral particulate mea~
surement literature was undertaken to resolve the confu-
sion of measurements presently surrounding the determi
nation of particulate contamination in parenteral prepa~
rations and to provide an informed basis for an action
plan. Relevant information from a thorough search of the
scientific literature was combined with current responses
from cach insrument manufacturer and some significant
preprints from the recent PDA sponsored “International
Conference on Liquid Borne Particle Inspection and Me-
tology.” This combination of information was utilized to
assure that any conclusions reached would be based on
current particulate measurement capability
The principal problem addressed in this review is the
lack of agreement in any of the available measurements of
particulate contamination required for the release of par-
enteral products. This critical problem is the result of a
combination of factors, most of which can be traced to
instrument limitations.
‘A major problem shared by all available systems is
created by the low sample volume handling capacity
which in turn imposes sampling errors on the required
tests. In the case of actual particulates with widely varying
particle densities, the variability is magnified. Thesé er-
rors can be identified as due to:
1, Sample preparation prior to measurement.
2. Losses in the handling of sample particulates within
the instrument.
In addition to the loss of particulates due to sample
‘manipulation before and during analysis, each of the sys-
tems now available suffers in some degree from:
1. Shape dependant signals,
2, Inadequate particle size range.
3. Specification of inappropriate measurement limits,
i.e. the number of particles counted are 100 low for
“This work was funded bya grant irom the PDA Research Commitee
Vol 42, Supplement 1988
measurement accuracy or the concentration of parti-
cles is too high for sensor capability
A shared problem in all available systems is the inabil-
ity to distinguish between particles, microbubbles and
insoluble microdroplets. The microdroplets can usually be
traced to the use of silicone oil as a packaging component
lubricant or to plasticizer droplets that have been extract-
ed from flexible parenteral packages. The microbubbles
are created in the liquid by either mechanical cavitation or
by the thermal release of entrained or absorbed gases.
While the small volume handling capacity is a major
problem, there are also errors imposed by the sensing
means employed. For optical sensing systems, flow prob-
lems in the sensing zone will result in random orientation
of particles traversing the sensing slit which, for other
than spherical particles, results in random selection of the
particle dimension measured. The variability imposed by
this effect is greatest for flakes and fibers. The results
reported by the Coulter instrument start with a volume
proportional electrical pulse which is generated as parti-
cles pass through a precision orifice in an electrolytic
solution. The particle signal is then processed to obtain an
equivalent spherical diameter. The volume signal is re-
ported to be less affected by particle position than the
‘equivalent optical signal as the particle passes through the
sensing zone. The volume measurements of the Coulter
system, however, yields equivalent spherical diameters to
describe even flakes and fibers. These equivalent diame-
ters are small fractions of the required major particle
dimension measurement
U. Common Factors
An essential requirement for measurement comparabil-
ity is that the capability of the devices employed be
matched in all significant parameters. This match, in
particulate measurements, must commence with the re-quirement that the detectors employed have identical ca-
pabilities in sizing and counting in the specified size range
This includes particulate concentration capability as de-
termined by the onset of a specified coincidence error, say
5%. Without this match in measurement capability the
evaluation of even ideal suspensions on otherwise ideal
instruments will not yield comparable results. The two
parameter match requirement can be met by any of the
particulate measurement systems in current use according
to published specifications. This requirement is as basic as
the specification of magnification in the section describing
the membrane/ microscope and, similarly, should be listed
in the USP XX1 (788) procedure (163).
The achievement of data comparability begins with
matched detector performance but cannot be accom-
plished with this single prerequisite. Comparable data can
only be achieved by a specification of rota! instrument
system performance requirements; these should be inctud-
ced in the (788) procedure. In addition to the publication
of these specifications, GMP measurement and certifica-
tion of system efficiency through the specified particle
size and density range should be required prior to use.
Historically troublesome areas have been technique
and sampling. Trasen (68), in his discussion of analytical
techniques for particulate matter, concludes, “In order to
keep sampling errors at a minimum it is important to
sample directly from the final packaged container and to
sample the entire volume” (emphasis added). Although
Trasen was discussing particulate measurement errors in
the membrane microscope technique his comment is fully
applicable to any of the other measurement techniques
discussed.
Since the (788) procedure involves sample pooling and
‘manipulation, an essential requirement for analytical ac-
curacy is suspension homogeneity. A major factor in the
accurate manipulation or transfer of liquid borne particu-
lates is their settling time, This is illustrated in Table 1
which lists terminal settling velocities for latex. glass, and
stainless steel microspheres in still water at 20 °C.
Prior to any discussion of Table I results, specification
of the required response range for this destructive test is
essential. What boundary should be considered for the test
limit stated in an open-ended way as >25 um? If the
Pharmacopeial intent is to provide gap-Iree particulate
quality assurance from 10 um upwards through the visible
inspection range, a workable solution can be defined.
TABLE 1. Stokes Law Computation of Terminal Settling
Speed for Spheres in 20°C Still Water, mm/sec
“Terminal Setting Speed,
Particle sm sec
Diameter, Stainless
am. Latex Glass Steel
10 0.0029 0.38
28 ois 238
50 0.072 9.30
100 0.29 38.00
200 TISisaae 152.00
Densities Catex = 1.05, Borosilica 57. Type 303 Stanien.
Steel = 786,
36
Knapp (166), using production tine rejects, selected repre-
sentative particulates for holographic measurement. With
this methodology, he defined 100 zm as the smallest pro-
duction line reject that an experienced inspector, without
using magnification, can detect 70% of the time. Borchert
(167) used prepared standards with precision fluorescent
dyed microspheres. Prior to experimental use, the quanti-
ty of microspheres in each container was verified under
UV illumination that made each microsphere a point
light, thus achieving a detection probability of 1.0. Fol-
lowing verification, well designed experiments using stan-
ard inspection illumination resulted in data which sup-
ported the visibility finding for 100 um. In the face of their
studies, data from the destructive tests, covering the range
from 10- to 100-sm particles, will supplement the nonde~
structive visual or optical particulate tests, with secure
data from 100 um upwards, to provide gap-free particu-
late quality assurance testing for parenteral products. To
assure realization of this range of data from either optical
ot resistance modulation instruments, such as the Coulter,
requires information on the effect of the various densities
normally encountered over the full size range being con-
sidered,
Accepting the 100-um size as an upper limit for the
(788) destructive tests provides a basis for review of the
Table I data. The 8.71 mm/sec terminal settling speed for
100-um glass spheres and the 38.00 mm/sec terminal
seitling speed for 100-m stainless steel spheres define the
agitation speeds required for the maintenance of uniform
suspensions. They also establish the length of time in
which an unstirred solution can still be considered reason-
ably uniform. Close consideration of the agitation limits
implied could suggest that total container sampling is a
more practical response
Addressing the case of actual particulates in test solu-
tions where particulate densities and sizes cannot be speci
fied prior to test, handling must be controlled to maintai
adequate suspension of the worst case particulate that can
bbe encountered. In the usual case, it is at least the han-
dling (both in agitation and operation speed) that will
keep glass particulates in suspension. At present, the
(788) pharmacopeial processing is such that errors ean be
introduced in the act of combining container volumes,
extracting the required aliquot, aspirating the sampled
volume into the liquid handling system, and finally effect-
ing movement of those particles through the sensing zone
of the instrument that have not been trapped on tubing
walls or in eddy currents. Vigorous agitation, just under
that for which cavitation results, will reduce the nonuni-
form sampling error; but the residual volume left unana~
lyzed in the instrument sample container remains a proba-
ble error source (175).
Inadequate flow velocity, the length, material, and cur-
vature of the tubing in the sample handling system be-
(ween pickup and measurement point contribute to the
loss of the larger and heavier particles. The recent FDA,
side-by-side test (179) of particulate measurement sys-
ems showed that the Climet system (180) with liquid
processing rate of 100/mL per min (compared to ranges
from 4.6 0 20 mL/min for the other instruments tested)
Journal of Parenteral Science & Technologyhad significantly better carrying capacity for the larger
particles than most other units evaluated. Settling and
trapping errors, even for 10-um latex spheres used in
instrument calibration, have been reported by Grant
(174).
In the recent past, the contamination resulting from
Kraft paper use in sterile areas has been eliminated by the
introduction of plastic packaging materials. However, the
use of plastic materials has brought with it a correspond
ing increase in “floaters”: particulates with densities low
enough that they can be trapped in the meniscus of the
solution. Since current systems and standards do not ad-
dress this problem, it could also contribute to data vari-
ability.
‘A common problem in all fluid stream particulate mea-
surement systems now available is their departure from
the Pharmacopeial required measurement of maximum
linear pasticle dimension. Both optical and resistance
modulation measurement can accurately determine
spherical and near-spherical equivalent diameters. The
Physiologically important measurements of flakes and fi-
bers can, however, be in gross error. It has been argued
that given knowledge of the shape of the particulate that
should be evaluated, calibration adjustments can be made
to obtain accurate results. The core problem with the
evaluation of production particulates in parenteral solu-
tions is that there can be no a priori description of the
particulates that may be encountered. Measurement dis-
crepancies resulting from shape differences, therefore,
remains errors, Problems can persist even with the avail-
ability of ideal analyzers: those inherent in the selection of
inappropriate limits for instrument operation, The statis-
tics of counting are well established. The establishment in
the (788) procedure of constant volume for analysis leads
to an error of 19.50% for a 95% confidence interval in
the determination of acceptance for the count of >25-m
particulates and 6.17% error in the >10-zm particulates
for the same interval. 95% confidence limit errors for the
‘SVI range from 'f 10 100 mL are shown in Table UI.
A review of Table II results clearly shows that a fixed
test volume specification is inappropriate for all container
sizes in this test. The error resulting from this source can
be controlled by the specification of a practical tora! error
limit. A tolerance of 5% for this measurement at the
maximum allowable particulate concentration for parti-
cles >25 um would define the test volumes required. Since
TABLE Il__Count Error for Fixed Sample Volume Determinations
this is a mandated limit test, accuracy at the compendial
test limits is essential for any review of the quality of a
tested bateh
Another measurement error (122, 175) that can now be
easily controlled is that due to the coincidence of multiple
particles in the instrument sensing zone. The magnitude
of the coincidence error is determined by the ratio of
particles to sensing detector volumes and is usually speci-
fied per mL of sample liquid. A review of the initial
analysis, therefore, permits the selection of any desired
error tolerance by dilution adjustment of the particulate
concentration. Delly's report (87) that 81 to 96% of all
particulates in some samples occur in the size range below
10 am where they can contribute, through coincidence, to
the data variability now seen, takes on added significance.
Incorrect batch rejections can result from these coinci-
dence errors which have been shown to be controllable
witha minimal change in measurement technique. A com-
plete derivation and discussion of coincidence errors is
included in Appendix II. It should be noted that the vol-
ume of the sensing zone in optical counters is a clearly
defined geometrical volume. In resistance modulation
counters, due to divergence of field lines in the three
dimensional liquid medium, the sensing zone requires em-
perical determination and is a multiple of the orifice vol-
ume. This multiple varies with the specific design chosen
and can range from 2.5 upwards.
Ml, Optical Systems
At the 1969 Liquid Borne Particle Metrology Confer-
fence sponsored by the New York Academy of Sciences,
two of the contributors were the High Accuracy Products
Corp. (109) and Royco Instruments, Inc. (118). These
Pioneers are now combined into the HIAC/ROYCO In-
struments Division of Pacific Scientific. Their basic parti-
cle detection concepts are still in use.
Both instruments were designed within the constraints
of the bulky low complexity electronics of the era and
functioned with minimal optical signals. HIAC selected
light blockage; ROYCO employed a somewhat more
complex forward scatter lighting principle. The surviving
design is that pioneered by HIAC. Most present instru-
ments follow the light blockage design concept pioneered
by HIAC. Particle passage through a narrow sensing zone
at right angles to the flow stream reduces the light energy
as Required in (788) Particle Counting
Particles X 10° 95% CA.
Pooled Pooled Tn 10 mb % Error
Volume 310 335 310 335 310 335
20 400 40 200 20 0.22 1.38
20 200 20 100 10 0.62 1.95
20 100 10 50 5 087 276
50 100 10 20 2 138 4.36
10 10 100 100 10 10 1 195 617
20 10 200 100 10 5 05 276 an
50 10 500 100 10 2 02 436 13.79
100 10 1000 00 10 1 a1 6.17 195
Vol. 42, Supplement 1988delivered to the detector. The signal generated is 2 de-
crease in sensor output proportional to the area of the
particle shadow projected on the photosensor. Far forward
seatter systems, such as the Royco, direct illumination
from the light source is blocked: only the light scattered by
the particle is, ideally, collected by a large area photosen-
sor. The amount of light scattered is proportional to the
area of the particle viewed by the sensor: the signal pro-
duced is seen as an increase at the photosensor output.
For both types of systems, only spheres can generate
signals independent of the orientation of the particle as it
passes through the photodetection zone. For spheres, the
‘mathematical extraction of an equivalent diameter can be
replicated with good accuracy. For irregular shapes,
platelets and fibers. the signal extracted varies randomly
with particle orientation as it passes through the detector.
The report of an equivalent diameter for these particles
cannot be related to the maximum dimension desired
without prior knowledge of the shape of the particle mea~
sured (88). When production particulates are considered,
it is clear that no effective particulate measurement is
possible except for spherical particles. In both systems
pulse height analysis was used to measure particle size
The basic design is well suited for low flow applications
Due to the relatively low sophistication level of the elec-
tronics, amplifier response time contributed to the mea-
sured coincidence errors,
In both systems random particle motion across the sens
ing zone, due to turbulent flow, limited measurement
accuracy 10 spherical particles. Flakes and fibers were
either measured with gross error or were disregarded if
the detected signal was below the threshold of the instru-
ment
The eighteen-year period since the 1969 meeting has
seen modular replacement of system elements. Today,
integrated circuits and microcomputers are in customary
use in cach of the commercially available particle measur
ing systems. With the availability of reliable, low-powered
as and solid state lasers, forward seatter augmented de
tection systems are once again in the marketplace
The two basic optical designs have been perpetuated
with little or no change in all present day systems. The
processed signal is limited by its primitive optical charac
ter and the turbulent flow conditions in the sensing zone,
The turbulent sensing volume flow randomizes the parti-
cle dimension scanned, thus limiting the utility of the
data
A. Filmy Materials
A major factor in the decision to use optical counters in
the US, was the existence of traces of the 5-HMF poly-
mer dextrose breakdown product in parenteral solutions,
Quoting from the 1980 July-August issue of Pharmaco-
peial Forum in which the following interim notice was
published, “For dextrose containing solutions do not enu-
merate morphologically indistinct material showing little
or nosurface relief and presenting a gelatinous or film-like
appearance. Since this material consists of sub-units of 1
zum or less in linear dimension and is liable to be counted
only after aggregation on the membrane
Following an industry collaborative study, the HIAC-
Royco was qualified as an alternative to the membrane/
microscope evaluation of parenteral particulates. AS a
result of this problem, Supplement No, 3 to USP XX
issued on February 15, 1982 excluded the 5-HMF poly-
mer particles from consideration as a rejectable particu-
late or allowed the use of an electronic particle counter.
The extension of optical counter usage from special pur-
pose tool to facilitate continued production of dextrose
containing solutions into its present usage as a device
considered usable for total particulate quality evaluation
in parenteral products had unfortunately not been ade~
quately studied prior to the commencement of its extend-
ced usage. Delly’s comments in this regard are especially
apropos (87). He evaluated the membrane/microscope
method of particulate analysis against the optical counter
and reported that thin filmy materials could be found in a
variety of apparent shapes and sizes in both methods as a
result of the handling that the film experienced. In the
electronic counter, thin filmy materials in the counter’s
turbulent flowstream could appear crumpled as balls,
scrolled up in needle or tubular shapes, and in flat or plate-
like appearance. He also commented that these films can
be substantially thinner than the wavelength of light used.
Under these conditions, little edge effect would be no-
ticed. Due to their gel-like nature, these particles tend to
take on the refractive index of the medium in which they
are immersed. To quote from Delly: “Presented edge on or
fore-shortened to the detector, these particles still have
some absorption color and will be seen, but will be counted
in the smaller category.” Delly’s conclusion concerning
optical counters is as valid now as when originally pub-
lished. Iti in part, “. .. particles in solution have at least
some chance of being considered in all aspects, and al-
though still not perfect, at least this method is more accu-
rate where unusual geometries are involved.
B. Refractive Index Effects
A problem shared by all counters employing optical
detection is that particulates whose refractive index
matches that of the suspending fluid cannot be detected.
This problem has been discussed by Lloyd and Freshwater
(168) in the use of a HIAC instrument and summarized
by Russell (179). As Russell summarized Lloyd and
Akers data, a difference of 41.25% in refractive index
between particulate and solution is required to avoid this,
kind of refractive index limitation, Within this band the
resulting errors can overwhelm those due to any other
source,
©. Conclusions
There is unquestioned utility and economy available
from the use of the particle detection systems listed in
Appendix I for the monitoring of parenteral product qual-
ity. The present usefulness of these systems is limited by
inadequate specification of the instrumentation employed
and by the sample handling method described in the
(788) method of analysis. Blanchard and his co-workers,
(53) and more recently Barber (173) have observed and
Journal ot Parenteral Solonce & Technologyreported the serious error contribution that suspension
nonuniformity generates in the measurement of particu-
lates. Kushner (175) also discusses the serious impact of
sampling errors traceable to nonuniform suspensions,
Minimization of handling errors and losses, selection of
test volumes that will result in data within acceptable
error limits and avoidance or reduction of the error result-
ing from coincidence will reduce the present range of data
variation seen, Pulse height analysis, now uniformly em-
ployed in optical detection systems, limits the maximum
size of particles that can be measured. In addition, particle
shape and the refractive index difference between particle
and suspending liquid will affect measurement accuracy.
Prior tose, the refractive index difference between parti-
cle and suspending liquid must be shown to be more thatn
£1.25%. In addition, Schroeder and Deluca observed
that calibration with similar shapes must be utilized to
obtain best results (89), The available optical particulate
analyses systems are therefore suitable for relative indica~
tions of product quality.
IV. Resistance Modulation Systems (Coulter, etc.)
At the 1969 Conference, Kinsman (93) noted that,
“particle counting is not easy but it can be done.” The
instrument Kinsman discussed followed Coulters original
patent by 16 years. While improvements have been made
in the Coulter counter over the years, the basic concept
unaltered. A cylindrical orifice in an electrolyte wi
change resistance as individual particles enter the orifice
displacing current conducting electrolytes. The output
signal pulse is nominally proportional to the volume of the
particle as it sweeps through the orifice. Since its intro-
duction, the Coulter has become the analytical instrument
of choice in diverse areas from blood analysis to the evalu
ation of industrial powder sizes; specialized adaptations
have also been used to evaluate fiber lengths. The present
availability of integrated circuits and microcomputers has
reduced the instrument size and increased its capability
‘The change from a constant voltage system to a constant
‘current design and the inclusion of a flow transition zone
at the orifice throat appears to have extended the particle
size range for linear response that can be achieved with a
single orifice. Linearity of sphere measurements up to 77
10 80% of orifice diameter were shown to be possible (106-
108). Coulter's conservative choice of new limits are from
2 t0 60% of orifice diameter; the older limits were 2 to
40%. The conservative 2% lower particle size threshold is
established by the electronic instrument noise: operation
to.1'4% is often possible
A. Shape Sensitivity
Resistance modulation instruments have evolved from
empirically defined devices to those whose response can
now be analytically calculated (100). The special chal-
lenge that must be evaluated in the analysis of parenteral
particulates is that the capability of this type of instru-
‘ment must respond equally to the full range of randomly
occurring contaminant types and sizes. The only particu-
Jate measurement specified in the XX] Pharmacopeia isin
Vol. 42, Supplement 1988
the membrane/ microscope procedure for LVI. USP XXI
uses the effective linear dimension. This selection is be-
lieved to be based on the potential blood vessel blocking
capability of particulates. The capability of these instru-
iments to generate the required measurement is discussed
below.
Karuhn and co-workers (95), reviewing pre-1969 expe-
riences with the Coulter, reported that they and others
experienced significant broadening of the distribution of,
latex calibration spheres over that determined by Dow
Chemical using a microscopic technique. Karun also
quoted experienced Coulter operators as saying that
“mass balances performed on various types of industrial
powders (ic., mass calculated to have passed through the
orifice to the mass determined by a weight difference)
generally was in the order of 1.31:1 for nonextreme shapes
while in the case of flakes it was often greater than this.”
Davies and co-workers (97) have shown that excepting
spheres “particles of identical volumes but different
shapes generated different pulse heights depending on the
magnitude of their approach diameter to the orifice.”
Experimental data indicated that the pulse height is also
dependant on the flow streamline followed by the particle
through the sensing zone (95, 97). Since flow in the sens-
ing zone is turbulent, data scatter results
It must be appreciated that Davies based his conclu-
sions on experimental data from a scaled-up model of the
Coulter orifice. This analog model was used due to the
‘complexities which are encountered in analysis of electri-
cal conduction in a three-dimensional volume. Davies also
investigated the effect on the pulse height of the volume
signal for orifice entry positions of varied shapes with
equal volumes. His data shows a marked proportionality
between the approach diameter of the particle and the
recorded signal. Of special interest is the difference in
signal reported for a rectangular shape with orifice entry
both in the flat and end-on positions. The signal ratio for
these two conditions is 3.37/1.49 = 2.26. The diameters
recorded for these two measurements will vary by 31.2%.
This is the kind of variability that is possible in lake and
platelet measurements due to this effect alone. When a
cube and sphere of equal volume are measured in this
system, the diameter recorded for the cube will be 1.8%
‘ereater than that for the sphere.
Lloyd (101, 102) also used a large scale analog of the
Coulter-type system to demonstrate volume linearity for
differing particle shapes traversing the orifice on a central
streamline. The volume measurements were linear within
the same particle shape but the slopes of the straight lines
relating volume to signal magnitude differed as particle
shapes differed. For the limited number of cylindrical
shapes investigated, the linear slopes varied from 0.70 to
2.49 of the spherical calibration curve slope (101). When
Lloyd studied @ range of shapes closer to spheres he found
4 range of linear slopes from 0.85 to 1.37 of his spherical
calibration curve,
Some of Lloyd's cylindrical shapes had proportions
similar to those encountered in fibers (i.e. length/diame-
ter ratios of 5:1, 6:1, and 7:1). In his studies, the cylinder
traversed the measuring orifice on a central streamline.
80TABLE III. Review of Fiber Measurement Effects on Resis
Example: Sum Diameter
Analog Mode, K,= 1.38 Physical Dimen-
Mag. Factor =(K) sion, Magnified L(USP XX1)
ylinder
Lid Ke Ky ik) ODD
1096 0.70 089 335 298
2 160 116 108 422 443 100
3196 12 112 483 SAL 15.0
4 234 169 119 531 632200
527 197 12s $72 11s 280
6 308 220 130 608 790 © 300
7 344 249 135 640 Bos 350
s 359 260 138 669 923400
o 395 280 142 696 988 450
Wor 421 305 145 721 1043500
20" 640 463 1.67 9.09152 100.0,
To illstrate this effect, measurements on a Sam diameter fiber of
varied lengths are compared with the USP XXI requted dimension
showing large differences. This magnification partially compensates for
‘he minimization of fiber length i his typeof measurement. The analog
‘model datas from Lloyd (101, 102):theastershed data ws extrapolated
‘The extrapolation i used on the bass of the linearity of the Tog/log
plot of slope against the ratio of fiber length to diameter
‘Notations:
per diameter Kk
phere diameter
magnified sphere diameter Ly
Kj =slope flinear fiber volume
curve vs, signal ouput
= normalized fiber
volume slope
Tength of fiber
linear dimension
/) = linear dimension
magnifier
Table {11, calculated from the physical dimensions and
Lloyd's data, shows that a fiber with a length/diameter
ratio of 5:1 will be evaluated as 125% of the fiber length
determined on an equivalent volume basis. Considering
the linearity of Lloyd’s data, results have been extrapolat-
ced to include length/diameter ratios up to 20:1. At 10:1
length/diameter ratio the extrapolated data shows a fiber
length magnification of 145%, Similarly, at 20:1 length
diameter ratio Table III shows fiber length magnification
of 169%. This magnification compensates in part for an
otherwise drastic undersizing of fibers in resistance modu-
lation systems.
Lloyd's data is limited t0 the examination of fibers
traversing the orifice on a central streamtine. Considering
the turbulent nature of low through the orifice and the
consequent randomness of both fiber position and path
during the traverse, Lloyd's work cannot be considered
definitive analysis of fiber measurements in Coulter-type
systems. An additional limitation that should be noted is
that the geometry of Lloyd's analog system was not mod-
eled after a particular commercial device, therefore, the
resulting magnification ratios can be expected to show
variation as orifices with varying diameters and lengths
are employed
B. Filmy and Porous Materials
Coulter-type measurements of filmy or porous materi=
als should also be considered when parenteral contami
nants are evaluated, In measurements of porous materials
10
(nylon and fly ash are examples) the dimensions recorded
are several times that due to the skeletal volume of the
particle (91). Filmy gels such as those encountered in the
5-hydroxy furfural glucose breakdown product are detect-
ed in Coulter-type systems on the basis of electrolyte
displacement, For instance, a mass equivalent to a 25-zm
sphere with solids content of 5, 10 and 20% will generate
volume signals respectively of spheres with diameters of
9.2, 11.6 and 14.6 um. It can be deduced that the essential
difference between these materials is the relative displace-
ment of electrolyte. The low solids content of the filmy gel
can generate signals below the noise level of the Coulter
instruments for smaller particulate volumes.
C. Sample Handling
The Coulter uses a cylindrical orifice, whose length is
about 75% of its diameter, to generate the particulate
signal. The orifice size specified for pharmaceutical prod-
uct testing has high fluid resistance due to its small size.
At the recent FDA tests (178) the flow rate recorded for
the Coulter instrument was 4.6 mL per min which was the
lowest flow among the instruments compared; the highest
‘was 100 mL per min, This low flow rate can be compensat-
ed for by vigorous agitation within the instrument to mini-
mize selective elimination of larger particulates prior to
their evaluation. Using an earlier model of the present
Coulter, Bungay and Krebs (92) reported that stirring
rate variation caused a 20% increase in count when higher
stirring speeds were used. Concerning the need for vigor-
‘ous agitation to avoid this error, Lines (181) comments as
follows: “the standard two bladed stirrer operating at
1020 rpm ina flat bottomed sample container will suspend,
40-um glass spheres in a saline solution.” Lines cautions
that irregular shaped pieces of glass may require different
agitation velocity to achieve the same results. The stan-
dard two bladed stirrer operating at 900 rpm in a special
round bottomed accessory beaker can suspend glass
spheres of 200 am diameter. Lines concludes that for 300-
‘zm glass spheres the Coulter four-bladed stirrer operating
«at 1320 rpm in the accessory round bottomed beaker with
vertical baffle is required to maintain suspension unifor-
mity, If consideration is extended to include suspension of
the occasional stainless steel fragment that may occur,
Stokes law estimates indicate 92-um stainless steel capa-
bility when 200-1m glass spheres are suspended and 138-
mn stainless steel capability when 300-zm glass spheres
are adequately suspended. Without adequate suspension
these particulate measurements cannot be made. Consid-
ering the irregular nature of particles in parenteral prod-
ucts, agitation to suspend at least the 200-um glass
spheres would appear to be a conservative choice of opera~
tion to ensure measurement of the occasional heavier par-
ticles that can appear. The agitation required to maintain
uniform suspensions of the wide range of particulates
‘encountered has not been adequately addressed and is a
problem for all types of particle analyzers in present use.
The agitation must, however, be below the limit at which
cavitation occurs since bubbles are counted as false partic-
ulates. Lines (103) reports that the Coulter counter re-
Journal of Parenteral Science & Technologysponse can theoretically be affected by particle shape,
resistivity, ete.: *...it is recommended that the instru-
‘ment be calibrated with the material under test.” In the
usual circumstances of product testing, neither the size
range nor the material of the contaminants are known,
Test data, as with the optical systems discussed, are suit-
able for relative indications of product quality. The
present design cannot be considered as approaching the
functional requirements for a referee method,
D. Conclusions
Based on the particle measurement used is USP XI
(163), the signal generation and computations used by the
present Coulter particle analyzer generate excellent to
usable measurements for spherical and near spherical par-
ticulates respectively. Measurement of flakes, platelets,
and fibers have been found to generate variable data. In
this type of measurement, an equivalent spherical diame-
ter is computed from a pulse height measurement of the
particles volume, The measurement of nonspherical parti-
cles have also been shown to be affected by the profile of
the particle as it enters the sensing zone and the stream-
line followed through the orifice. Inadequate detection of
filmy gels, such as those of the S-hydroxyfurfural glucose
breakdown product, must also be considered in any evalu-
ation of the present Coulter system (or its commercially
available equivalent) for quality assurance measurements
of parenteral particulates. The low flow rates in Coulter
type instruments require small volume sample processing
which increases measurement error potential. The avail-
able resistance modulation particle detection systems for
parenteral particulate analysis are, therefore, suitable for
relative indications of product quality.
V. Present Detection Systems
A. Comparison
Tables IV and V have been prepared to provide an
objective comparison framework for optical and resis-
TABLELY. Fiber Measurement Result Comparison for Opti-
cal and Resistance Modulation Systems Showing
Major Differences from the USP XXI Measure-
ment Specification
USP XXI
Fiber Physical Resistance Optical -—_Linear
11/4; Dimensions Modulation. Measurement Dimension
Ratio “de Lr Dm Dy DG DED
sl oS$ 2 98 123 5 126 25
10 $0 196 245 0 252 50
2 100 391 490 20 505 100
1 $30 123 178 5 178 50
10 100 247 388 10 357 100
2 200 493 715 20 714 200
21 5 100 155 259 5 258 100
10 200 311 519 10 505 200
20 400 62.1 1037 20 174 400
Notations
4; = fiber diameter
B_ » linear dimension
Dj = minimum optical measurement of equivalent spherical
diameter
‘D3 = maximum optical measurement of equivalent spherical
diameter
‘Day = resistance modulation equivalent spherical diameter based on
volume caleulation
Dig magnified fiber measurement showing effect of Lyd ratio
tance modulation particle measuring systems with which
parenteral particulates can be evaluated. In these tables
are listed typical nonspherical particulate shapes and sizes
that can be encountered in production material. Three
fiber groups with length /diameter ratios of 5:1, 10:1, and
20:1 are listed in Table IV. Relatively thin arrowhead and
square shapes have also been selected to represent chips
and flakes and are shown in Table V.
‘The performance of these particulates against the USP
XXI specified maximum linear dimension will now be
‘considered. For optical systems operating under the best
TABLE V. Measurement Result Comparison for Optical and Resistance Modulation Methods with Particle Shapes Representative
of Chips and Flakes Showing Major Deviations from the USP XXI Lineae Dimension
Resistance
Physical Dimensions Modulation USP XXI
article Shape t Lyla b Di in./max.) B ‘DE___Linear Dimension
Arrowhead 5 30 25 17.9(143/32.4) 178 218 50
15 100 50 35.9(33.5/435) 33.7 55 100
20 200 loo 71.8(57.4/1290) 7141110 200
Square 5 25 = 18.1 (14.5/32.8) 126 282 354
10 50 36.3 (29.0/65.7) 25.2 564 70.3
20 100 = 726 (8.11314) 50S 1128 14.4
Notations:
Like ‘= cqual sides of triangular chp shape o sides of square base of rangular chip shape
b base of triangular chip shepe
o minimum opis! measurement of equivalent spherical diameter
ob ‘aximum optical measurement of equivalent spherical diameter
Dom = resistance modulation equivalent spherical measuremeat based on volume calculation
Don (min, fax.
Vol 42, Supplement 1988
‘estimate of eect of particle orientation in traverse of sensing zone
sitconditions, that is with laminar flow conditions through
the sensing zone and with oriented particles, the dimen-
sions recorded are listed in the “Optical Measurement”
columns of Tables IV and V. The three groups of fibers
(5:1, 10:1, and 20:1 length/diameter ratios respectively)
are evaluated as 50, 35, and 25% of the required dimen-
sion. When the flow through the sensing zone is adjusted
to be turbulent, all positions of the fiber in the sensing
zone become equally probable and the spread of measured
values for the same sequence of fiber groups becomes: 20
10 50, 10 t0 35, and 5 t0 25%.
When resistance modulation measurements are con-
cerned, consideration of their variability begins with com-
putations of the diameter which will define an equivalent
spherical volume. These computed diameters are listed in
the column titled “Resistance Modulation.” When Lloyds
multiplier is used to estimate the dimension recorded for 2
fiber with a length /diameter of 5:1, the result is 49% of the
desired linear dimension. The extrapolated values for 10:1
and 20:1 length/diameter ratios are 36 and 26%, respec-
tively, of the USP XXI required dimension. Since orifice
flow is turbulent, additional measurement variability will
result from the randomness of the path followed through
the sensing zone (97). Since Lloyds data is not related to
any commercial device, the computations cited must be
considered crude estimates.
For the two shapes representative of chips and flakes
shown in Table V, the optimum optical results for the
arrowhead shape is 56% of the required dimension; simi-
larly, for the square shape 80% of the USP XXI dimension
is achieved. When turbulent flow through the sensing zone
is selected, measured dimensions for the arrowhead be-
tween 36 and 36% of the maximum linear dimension
become equally probable. Similarly, for the square shape,
fa range of values between 36 and 80% become equally
probable in turbulent flow. Examining resistance modula-
tion data for the chip and flake category of particulates,
for the dimensions of the arrowhead shape shown, the
spherical equivalent dimension evaluluated is approxi-
mately 36% of the USP XX1 dimension; for the square
shape listed the equivalent spherical dimension is 1% of
the size required. When the effect of turbulent flow on
particle position as it traverses the orifice is considered,
Davies’ (97) data on the ratio of rectangle flat and end-on
‘measurement variability can be used to estimate the effect
fon the measurement results. The results will, with equal
probability, be distributed as follows: for the S-m arrow
head shape 33.5 t0 43.5% of the desired dimension and for
the square shape 47.4 to 61.7%. An additional variability
of 3 to 5% is contributed to this data variation by the
random selection of the particles pathway through the
orifice.
B. Conelusions
Neither the resistance modulation nor the optical detec
tion systems surveyed evaluate the maximum linear part
cle dimension as described in USP XXI (163). In the
optical instruments available, measurements are based on
the maximum projected cross-sectional area of the parti-
sr
cle as it traverses the sensing zone. For a laminar flow
system delivering oriented particles through the sensing
zone, the measurements are simply related to the parti-
cles’ shape and are listed in the D*apica column of Tables
IV and V. No presently available system makes this type
‘of measurement. Instruments with fully developed lami-
nar flow in the sensing zone will deliver this type of mea~
surement for fibers and will show some degree of improve-
ment when chips and flakes are measured. When turbu-
Tent flow is encountered, the resulting randomness of
particle position in the sensing zone results in the full
range of measurements shown in Table IV from D-opict
to Depa with equal probability.
In resistance modulation systems, the simplistic as-
sumption that linear volume measurements forall particle
shapes is obtained with spherical calibration has been
shown to be incorrect. The divergence of field lines in the
electrolytic detection system used in these instruments
significantly affects nonspherical measurements. To the
extent that the data used in Tables 4 and 5 yield valid
estimates, the shape sensitivity of resistance modulation
systems increases the equivalent diameter of nonspherical
particles. The amount of this increase is such that for
nonspherical particles no clear superiority between optical
and resistance modulation instruments can be established
at the present time.
No present manual or automated system achieves ac-
curate measurements when filmy particulate materials
are evaluated.
‘The minimization of sampling errors can be addressed
by evaluating the total contents of containers. To achieve
this goal in practical terms requires improved sample
volume handling capabitity. When the presently available
systems are evaluated from this point of view, an impor-
tant benefit is seen in the design of the sensing zone of
optical detection systems. Fora given particulate concen-
tration handling capacity (Le., for a specified coincidence
error), the cross sectional area for flow of the sensing zone
of an optical instrument can be much larger than in the
resistive modulation system. This increase in cross sec-
tional area also minimizes the possibility of blockage dur-
ing use and generates less fluid resistance than the cylin-
drical Coulter orifice. For liquids with low cavitation
threshold or those with higher viscosity levels, the flow
resistance consideration may well guide the final choice of
instrument selected.
VI. Recent FDA Test Results
It is impossible to distinguish significant operational
benefits among any of the particle detection systems now
available in any search of the literature or as a result of
the side-by-side tests just completed by the FDA (178).
The only resistance modulation instrument tested was
the Coulter. The optical systems evaluated included: CLI-
MET, HIAC, KRATEL, and MET-ONE. The HIAC
was used with @ Russell Laboratories sensor. The particle
measurement systems unit was not included due to the
manufacturers’ scheduling difficulties. Appendix 1 in-
cludes details and comments for the listed particle mea~
Journel of Parenteral Science & Technologysurement systems. Each system listed uses modest modifi-
cations of the primitive optical design pioneered by HIAC
and ROYCO and discussed in 1969. Resolution and re-
producibility of size determinations are required in the
(788) procedure for 10- and 30-um particulates. Valida-
tion of the capability of each system over the full range of
particle sizes that can be measured with it as in a counting
efficiency determination, has been inadequately consid-
ered. This inadequacy in the validation could prove to bea
source of the troublesome differences between measure-
‘ments made by presumably comparable systems for >25-
um particles. Specifications for agitation during sample
handling and processing on the selected particle analyzer
are considered to bea critical prerequisite for data accuracy.
VII. Recommended Actions
A. Stop-Gap Proposal
The economic and regulatory value of the measure-
ments available from automated particle counting sys-
tems are generally acknowledged. With the sources of
data variability described above, some approximation of a
referee method is essential. This initial referee method can
be provided by the measurement of full container volumes
on systems with validated particle size linearity and reso-
lution from 4 to 100 um whenever the use of the present
sampling and handling described in (788) results in a
batch rejection.
B. Near Term
Materials and Techniques: Much could be done to im-
prove test result comparability with adequate recognition
of sampling errors and handling requirements necessary
to maintain uniform sample suspensions, The testing of
particulate measurement systems for equivalent perfor-
mance depends on the availability of identical suspensions
with precisely maintained homogeneity. Any differences
in either suspension constitution or homogeneity (when
solution aliquots are used) will reduce comparability of
test results. Data for particulate instrument system evalu-
ation cannot be in any closer agreement than the differ-
ences in the test suspensions employed for their evalua~
tion. Development of the techniques neccesary for the
preparation of standard suspensions and the maintenance
of their homogeneity is therefore an early priority.
It must be stressed that prior to the test of the instru
‘ments, the handling and sampling techniques required to
maintain sample accuracy from the container until entry
into the measuring device is an essential prerequisite
Containers prepared with selected spheres having the re-
quired range of density and size (say 200 um of glass) can
be used to develop the handling necessary to assure accu-
rate maintenance of suspension uniformity throughout
the required handling.
Instrumentation: When the necessary handling tech-
nique has been adequately described, the validation of
competitive detection systems can commence. Consider-
ing the importance of these tests to both the pharmaceuti-
cal industry and its regulators, the test protocol should be
Vol. 42, Supplement 1988
developed in cooperative interaction. The tests should be
comprehensive enough to establish the essential instru-
tment qualities required over the entire size and particle
density range required:
1. Sample handling capability.
2. Size resolution.
3. Size reproducibility.
4. Coincidence onset.
Enough testing to accumulate statistically valid results for
each of the systems in each category listed is essential. It
must be recognized that the time and labor required for
method development and testing are substantial. Any at-
tempt at a “quick look” isa disservice to the industry and
its regulators.
VIII. Longer Term Actions
For a longer time frame response, it is recommended
that specifications for a referee method system be pre-
pared. Following review and acceptance of these specifi-
cations, a request for proposal should be circulated to
selected vendors in a publicized, open competition, Evalu-
ation of the responses, tests of the developed system, and
the emergence of a secure referee method should then
follow in sequence.
IX. Future Perspectives
A. All Systems
‘As discussed, sampling the entire contents of a contain-
er would remove one major element that results in data
variability. For routine use, this requirement must be
supported by either higher sample handling capability
than is commercially available at present or methodology
which will reduce volume requirements by concentration
‘of the particulate contaminants prior to test.
B. Coulter System
A recent telephone discussion with Coulter's chief de-
sign engineer in England, R. W. Lines, revealed that
Coulter holds patents that could be used to evaluate the
maximum dimension in fibers and flakes as required in the
‘mandated particulate test. The design change requires the
creation of laminar flow stream through the sensing vol-
ume and detection of the passage times of particles
through it. A market request for the investment time and
labor to achieve this result has not yet appeared. Improve-
ment in the volume handling capability of these instru-
‘ments should also be considered.
C. Optical Detection Systems
There are two major deficiencies in the basic optical
signal presently used. The first results from the fact that
only a single imaging plane is used in the present genera-
tion of optical particle analyzers. With this limited capa-
bility, the dimension reported for nonspherical particu-
lates is randomly determined by the particles orientation
as it is swept past the detection slit and it, therefore,
seldom approaches the maximum dimension required. A
flake can be recorded as a sphere with its diameter deter-mined by the projected area presented by its thickness and
its length; the diameter reported will be. in this case,
substantially less than that required. When the flake tran-
sits the scanning slit in a perpendicular position, the di-
mension calculated can approximate the major dimension
specified in USP XXI. In the extreme, a fiber could be
reported as a sphere whose diameter is determined from
that of a dise equal to the fibers’ diameter. In each ease a
second viewing plane at right angles to the one in present
use could be used to improve the quality and information
content of the optical data, The second deficiency is that
due to sole use of pulse area particle measurement without
any use of transit time measurement. This type of signal
analysis limits the maximum length of particles that can
be measured to the sensor slit width, The use of transit
time measurement, however, requires control of liquid
flow conditions in the sensing zone. Alternatively, direct
measurement of particle size using the recent improve-
iments in imaging technology and computation in the right
angled viewing system described above could satisfy the
requirement for a standard referee method that would
provide information concerning three dimension particle
shape as well as its major dimensions.
X. Notes,
Appendix I lists commercially available particle mea-
suring system descriptions and comments.
Appendix I treats the problem of coincident count
error and reduces it to an easily avoidable problem in the
course of particulate measurements. An earlier version of
this paper was presented as part of the H. K. Kushner, L
Abramson, T. Barber, and J. Z. Knapp paper titled, “Im-
plications of Sampling Theory,” presented at the Interna
tional Conference on Liquid Borne Particulate Inspection
and Metrology, May 11-13, 1987.
Appendix 111 isan attempt at specifying a particulate
analysis system which will eliminate the concept limita-
tions discussed in this Report.
Appendix I: Commercially Available
Particulate Measurement Systems for
Parenteral Use—Descriptions and
Comments
Climet Instruments Co.. P.O. Box 1760, Redlan
92373 Model C1-1000
The Cl-1000 instrument with the C1 150-150 light obscu-
ration detector and the separate C1 1000 sampler unit
‘were among those evaluated by the FDA. The sampling
unit for small volume injectables uses a 10- or 20-ml
syringe to draw the sampled liquid directly through the
detector. This minimized path is believed to be the reason
for the outstanding large particle detection demonstrated
for this unit, The Cl 150-150 detector is designed for
operation up to particle concentrations of 4370/mL. with
5% coincidence error. A new three-fold higher concentra-
tion detector isin final development
CA
su
Coulter Electronics Inc, 13960 N. W. 60 St., Miami
Lakes, FL 33014 Model ZM/P
The Coulter Model ZM/P with 140-ym orifice was in-
cluded in the FDA equipment evaluation. The use of the
Coulter was aborted due to the lack of agreement between
its data and the other instruments present. Since the sig
nal processing method chosen for the Coulter yields data
in gross error for measurements of flakes and fibers it is
judged undesirable for the evaluation of parenteral partic-
ulates. The Coulter was the only nonoptical instrument
included in the evaluation: it employs resistance modula-
tion to detect particulates.
HIAC/ROYCO Inst. Die., Pacific Scientific, 2431 Linden
Lane, Silver Springs, MD 20910 Model 4103
‘The HIAC/ROYCO system recommended for contami-
ant monitoring in batch samples is their 4103 system.
‘This includes the Model 4100 counter, the Model 3000
syringe operated sampler and a selected detector for the
particle size range of interest. The recommended sensors
for (788) determinations are the HR-60HA for 1.5~30-n
particles or the HR-120HA for 2-100-y particles. Since
the HR-120HA provides gap free data when its data is
integrated with the results of a visual or nondestructive
optical inspection, it should be of greater interest. A flow
rate of £1 mL is specified with this detector to assure
specified accuracy. This detector has 5% coincidence error
at a concentration of 6000 particles/mL.
Kratel Instruments GMBH, D 7250, Leonberg, Stuttgart,
West Germany Boblinger Strasse 23
The Model 100 with the HIB light obscuration detector
was evaluated by the FDA. It is a small compact unit
using a stepper motor driven syringe sampling unit. The
fluidic design eliminates the pressure pulsations resulting
from the stepper motor drive. The short path length be-
tween sampling syringe and detector resulted in large
particle detection performance almost as good as the Cli-
mel. The detector design is very similar to that of the
Russell unit discussed below. It is rated for a concentra-
tion of 22,222 particles at a 5% coincidence error
Met-One Inc., 481 Grants Pass, OR 97529 Model 214
‘The Model 214 with the Model 211 detector uses forward
scatter light employing 2 solid state laser diode ina system
offering calibration automation. The benefit of the laser
use in the 5- to 100-x particle range is its 25,000-hr stable
lifetime, The detector is designed for a coincidence error
of Sat a concentration of 3390 particles/mL. A detector
with 10,000-particle/mL capability is in final develop-
ment. The Met-One Model 250 Automatic batch sampler
designed for use with this system has 10-120-mL sample
capacity and can apply either pressure vacuum as the
driving force
Particle Measuring Systems Inc. 1855 8. $7th Court,
Boulder, CO 80301 IMOLV/SOPS 100 System
Due to scheduling difficulties on the part of the manufac-
turer, this laser based instrument was not included in the
Journal of Parenteral Science & TechnologyFDA evaluation. This instrument operates with a maxi-
‘mum concentration of 3000 particles/mL for a specified
size range of 2-150 w. With the 10-mL. syringe mounted
on the sampler flow ranges of 20-168 mL/min are avail-
able. At these high Now ranges, superior large particle
detection performance is expected
Russell Laboratories, 3314 Rubio Crest Dr., Altadena,
CA 91001
Designs and manufactures light obscuration detectors
only. The FDA favors the RLV 1-50H Model for use with
their HIAC system, Model PC320. This detector uses a
tungsten source operated to provide extended life. The
design provides self-alignment when lamps are replaced,
The RLY 1-50H Model could be used with @ concentra-
tion of 22,222 particles/mL at which a 5% coincidence
error will occur.
Appendix Il: Coincidence Errors in
Particulate Counters
Introduction
The error in particulate size measurement due to the
simultaneous presence of more than one particulate in the
detector volume can be potentially troublesome. This er-
ror comes from evaluating a concentration of particulates
‘beyond the accuracy limits ofthe selected detector.
‘The presence of multiple particles in the detector vol-
‘ume results in the addition of the individual signals. The
coincident signal sum cannot be distinguished from the
signals of single, larger particles. These coincident signals
can contribute to the rejection of a batch of acceptable
material. This error can be easily recognized and avoided
The analysis below reviews this error and relates its mag-
nitude to the number of single particles inthe test solution
With this information available, the user can evaluate the
quality of the data being generated and can take correc-
tive action, when required, to maintain the degree of accu-
racy specified for the assay. The bibliography listed indi-
cates the troublesome potential of this problem (1-7)
Following a general treatment, coincident count error
ima detector with typical dimensions are computed. It can
be seen that examination of the initial count results can be
sed to determine the adjustment of particulate concen-
tration required for operation within any desired error.
The effect of a massive overload of particulates below the
range of clinical or regulatory interest is also examined.
Analysis
Expressing particle concentration/mL in terms of mul-
tiple detector volumes/particulate
C= 10" /nV,
where C, = particulates/mL, n = multiple detector vol-
umes/particulate, and Vg = detector dimensions in ym.
The average number of particulates to detector volumes
is designated lambda and is the reciprocal of
Vol. 42, Supplement 1968
d=1/n
Since the number of detector volumes/mL is large and the
ratio of particulates to detector volumes is fixed, the Pois-
son approximation can be used to analyze the probability
of particulate coincidence within the detector volume (8,
9). Expressing the particulate detector volume as K, the
probability of K occurring in such a volume is:
K (particulates/detector volume) = (Se™)/K!
Table A.I lists the results of using the commonly select-
ed ratio of ten cell volumes/particle. It can be seen that
over 90% of all cell volumes are empty, approximately 9%
have single particles, 0.45% have two particles, and
0.016% have three particles in them
It is convenient to have an expression for the sum of all
possible coincidence effects for any selected operating
condition. Since the sum of all terms in the series, from
zero to infinity is 1, deducting from | the probability of an
empty detector and that of one particle/detector, results
in the total number of coincidence occurrences for a se=
lected ratio of particles to detector volumes; it is:
K(T) = 1% de®
=1-e%U +d)
In Table A.t, the computations are based on ten cell
volumes/particle (or 0.1 particle/10 cell volumes). The
sum of all coincidence combinations is 0.00467884. This
sum is only 3.42% larger than the two particle coincidence
probability of 0.00452419 as shown in this table.
The probability of multiple particles in the detector
volume increases with particle count. The coincidence
effect is expressed as a ratio of multiple particles counted
to those of the single particles in the solution. These ratios
are shown in Table A.II
‘A convenient way to utilize these results is to evaluate
the coincidence effect errors in a detector of typical di-
mensions. Selecting typical dimensions 100 X 100 X 1000
jum and calculating the coincidence of two and three parti-
cles in the detector as a percentage of the single particle
‘counts. This has been accomplished in Table A.{II. The
final column in Table A.III lists the sum of all coincident
‘counts as a ratio of single counts for the particulate con-
centration selected.
For the selected detector volume, coincidence errors are
seen to increase with increasing particulate concentration
as shown by cither the values of decreasing n or increasing
lambda. Review of the data in the last three columns of
‘Table A.JIL show that the greatest error contribution is in
TABLEA.L Probability of Zero, One, Two, and Three-Parti-
ee
Coincidence Probability of
Keparticlesin ny Remarks
090483742 Empty detector
0.09048374 One particle
0.00852419 Two particles
0.00015081 Three partcies
= General case
815TABLE All.
Counts to Single Particles
General Solution for the Ratio of Coincidence
NO) e* Ld Zeroes Ratio
NI) Ae
NQ) . Net/2 Ld Doubles Ratio.
NO)” de? 2
NG) eA/6 ‘Triples Ratio
MI) deh 6
Ae Ko D jeneral Ratio
See General Rati
TOOFM LUE gy Coine
de a cidence Ratio
TABLE A.lII. Coincidence Errors Expressed as a Pereent of
Single Particle Counts for a Detector Whose
‘Volume is 10? um?
(NQ/NDNGY/NI) NTNU
Lambda ER = Rnb
5 0.20 20,000 10.000 0.667 10.701
10 0.10 10,000 5.000 0.167 5.171
2 008 000-2800 0042 2.542,
50 002 2,000 1.000 0.007 1.007
too 0.01 1,000 0.500 0.002__—0.502
the coincidence of two particles. Three particle coinci-
dence is at least an order of magnitude smaller. The last
column, showing total coincidence error, is very litle dif-
ferent than the combined error due to double and triple
coincidence.
For a detector with half the volume of the detector used
in Table A.IIL, the particle concentration values for the
same error are twice those shown, For a detector with
twice the volume of this detector, particle concentration
values are half those shown in the table.
In the example of Table A.IIl, Ro, Rs, and Rr are
expected ratios which will be seen as an average of many
trials. Due to the small count numbers that these ratios
determine for double and triple coincidence counts, the
95% C.L. limits can be large. As an example, when 1%
coincidence operation is selected from this table a maxi
mum concentration of 2000 particles/mL. is shown to be
the measurement limit. The 95% confidence limits for a
count of 2000 particles in 1 mL is 4.36%. The 0.007%
‘occurrence of double coincidence for this example shows
that only 14 double coincidence counts will occur in a 1-
mL sample volume. For this small number of particles
counted, a wide 95% confidence limit results; in this case,
452.9%.
One requirement for data uniformity is the selection of
a specified coincidence error at a particulate concentra~
tion designed for the mandated test. The (788) test speci-
fications as presently written require measurement capa~
bility to 20,000 particles/mL for evaluation of Ys-mL
containers. This measurement requirement is commer-
cially available, The technical soundness of this test speci-
S16
fication is beyond the limi
The relationship between coincidence errors and parti-
cle concentration shown below has been extended to in-
clude the effect of massive concentration overloads of
particulates well below the range of clinical or pharmoco-
peial interest. This type of concentration overload might
result as a consequence of the extraction of plasticizer
from parenteral bag material
In an extreme case, n could well be equal to 1. For
clarity in the following discussion, the diameter of the
interfering droplet is assumed to be | zm. The concentra-
tion of these droplets, for the detector used in the example
above, is 100,000/ml.. The coincidences resulting and the
effective diameter of the merged particle are shown in
Table AV.
The effect of coincidence on the evaluation of particle
size varies with the type of detector employed, For Coulter
counter type instruments, the particle volume is measured
and the diameter is calculated from the sensed volume.
The total particle volume resulting, ¥, is:
V, = w(D,/6[1 + (D,/D)'1
of both reason and this analy-
where D; is the particle diameter and Dz is the diameter of
the interfering droplet. For a ratio of 10:1 between these
diameters, the measurement effect is negligible.
For optical counters, particle size is evaluated by mea-
surement of the projected area of the particle. The coinci-
dence effect can be calculated from the sum of the areas
involved, The total area, Ay,
A,= (DY /4{1 + (Dy/D,)")
where D, and Dz are, as above, the particulate and the
droplet diameters, successively.
The effective diameter of multiple coincident droplets is
examined in Table A.1V where the slow rate of increase of
the effective droplet coincidence signal is clearly evident.
‘The effect ofthe coincident signal on the measured diame-
ter of 10- and 25-zm particles is examined in Table A.V
for both the increase in size and the probability that this
increase will occur given the volume of the detector and
the concentration of 10,000 particulates/mL chosen for
this example.
In Table A.V it can beseen that the disturbing effect of
the droplets on the measured diameter of even the 10-zm
diameter is negligible, When 2 doubling of the initial
TABLE A.IV. Coincident Count Effects for Massive Over-
load of I-um Droplets. Detector Volume 107
1am? Droplet Concentration 100,000/m
Normalized Equivalent
Count Ra Count __Diameter, nam
y= Na/N, = 0.500 50,000 1at
0.166 16,667 13
0.0866 a6 2.00
0,00833 833 223
R 0.00140 140 244
R 0.00020 20 265
Ry = Ne/Ni = 0.000025 25 2.83
Journal of Paranteral Science & TechnologyTABLE AY,
‘The Effect of an Overload of 1-um Droplets on
the Accuracy of Measurement of 10-and 25-um
Particles and on the Probability with which this
Increase is Observed
Coincident Equivalent Probability
Lum Diameter, Size Inerease,% of
Droplets TO um 254m Increase, %
1 1.000.499 0.080 36.788,
2 141 0.995 0.160 18.394
3 173 1490239 6.131
4 200° «19803191833
3 223 246 03970307
6 244 293 0.475. 0.051
7 265 3.450.560 © 0.0072
8 2833930639 0.0009,
droplet diameter is reached and coincidence witha 10-zm
particle measurement occurs the effect is seen as a 2%
increase in measured size. When the coincidence effect on
25-uin particles is considered the effect is considerably
smaller; the increase due to the doubling of the droplet
signal to 2 um increases the measured diameter by
0.319%, Even at the eight-fold coincidence shown in this
table, a projected occurrence of 1/100,000 in this exam-
ple, the measurement effect is seen to be only 3.93% at 10
hm and 0.693% for 25-um particles. As the coincident
Groplet signal grows in size, the probability that it will
affect computational accuracy is seen to rapidly diminish
Iti, however, reasonable to expect that there could be
droplet growth during product storage and consequent
effect on the controlled particulate size range. This discus-
sion has also neglected the possibility that turbulent flow
conditions in the sensor could lead to inelastic droplet
collisions and, therefore, droplet growth during measure-
ment,
For those who considered particulate analysis in the 2-
to 5-zm region to be an adequate indicator of the particu-
lates below the mandated measurement span, this has
clearly been shown to be ineffective. A choice between
data from laser-based instrumentation or chemical analy-
sis for quality assurance control of this condition appears
tobe indicated.
The presence of particles below 5 um in major dimen-
sion, while of interest as process control indicators, are not
of pharmacopeal or present clinical concern, The data
analyzed in Table A.IV supports the conclusion that the
‘major effect of high concentrations of particle in this size
range would be a distorted analysis of particles in the 5.
10-1 range. This distortion is unlikely to affeet the com-
pendial test results.
Error contributions from particles between S and 10 jm
can be counted as double or triple their correct size and
thus enter into the controlled count of particles greater
than 10 um. Those particles in the size range between 10
and 25 wm have greater potential effect on compendial
measurement limits than the I-zm droplets whose effect
has just been reviewed. Coincidence errors in this size
range should be regarded with concern since the control
limit is ten-fold lower than that for the smaller particles
ol 42, Supplement 1988
For instance, the coincidence of two particles over 17.73
um in diameter will result in the detection of a 25-um
particle signal. Other particle pairs in this size range
whose coincidence will result in a 25-um particle signal
are: 3 and 24.82, 4 and 24.67, 5 and 24.5, 10 and 22.9, 15
and 20.
Conclusions
The effect of the error in particle size evaluated duc to
concentration has been reviewed. The range of particle
sizes that can contribute to this kind of error is from 5 to
those less than 25 um in major dimensions. The false
transformation of particle sizes merits careful consider-
ation and adjustment by dilution when it occurs. Theonset
of this kind of error can be determined by a review of the
concentration of particles measured in the test solution
against data such as in Table A.III. The methodology
described facilitates selection of particulate size analysis
within any selected coincidence error limit. Particulate
‘measurements that exceed a specified error limit from
coincidence effects should be considered invalid. This is
especially so since it is impossible to deduce a valid
correction factor and avoidance of the error is so simple.
The analysis and conclusions presented are valid for
‘those suspensions in which the distribution of particulates
can be adequately described as an average per unit volume
of liquid, This requirement can only be satisfied by sti
ring of the solution through the entire measurement peri
‘od at a rate to achieve suspension of the full range of
particle sizes and densities to be found within it. The
absence of any review of the rate at which particulates
enter the detector can seriously impair the accuracy of the
‘measurements that have been made. A system adjusted to
operate with a 5% coincidence error when the solution is
well stirred can achieve an unacceptable 25% coincidence
error if the particulate burden is concentrated in the last
20% of the solution to be evaluated because of sedimenta-
tion. Considering the present lack of attention to this
problem it may well multiply the major sampling errors
that have been recently described (10).
Acknowledgments
Dr. Lee Abramson’s clarity and helpfullness were es-
sential to the ideas presented in this paper.
Bibliography
1, Wales, M, and Wilston, J. Ni, “Theory of coincidence in particle
eounters." Ree. Set. Instrum, 32(10), 1132 (1960)
Kubitschek, H. E, “Loss of resolution in Coulter counters,” Reo
Sei Instrum, 383), $16 (1962).
3, Berg, Rober I, “Sensing zone methods in fine patil size analy
sis" Mat Res. Standards, 83). 119 (1963)
4. Prince, L. Hand Kwolek, W. F., “Coincidence corrections for
parle size determinations with the Coulter counter,” Rev. Se.
Instrum, 36 646 (1965),
Pisani, JF. and Thompson, G. H., “Coincidence corrections for
parle size determinations with the Coulter counter” Ret. Sc
‘rsa, 36,634 (1963).
6 Lieberman, A. "Flow rate and conentaton effects in automatic
patil counters” Proc. Natl. Cov. Fluid Power, Chieago (1975)
17, Raaseh, 1 and Umbaver, H.,“Ertors inthe determination of par-
tcl see dsteibutions caused by coincidences in optical particle
counters” Pert. Char. 1 85 (1984),
878, Personal communication, Lee Abramwon, Statistical Consultant,
Wastington, D.C
ipele, R.- and Myers, R., Probability and Statistics for Eugi-
inert and Scientists, 2d ei, MeMillan Pub, Co. Ine, New York
NY. 1978,
10, Kushner, H. K. Abramson, L. Rand Knapp, 1.2. "Implications
cof sampling theory,” Presented atthe May 1987 Meeting on Liquid
Borne Particle Inspection and Metrology in Washington. D.C
Appendix Ill: “Ideal” Particulate
Measurement System
‘The “ideal” Particulate measurement system described
below is, necessarily, a compromise. The specifications
are a balance between capability and cost increase. They
have drawn heavily on the best that has been achieved in
the commercially available instrumentation and have in-
cluded extrapolations that would add additional desirable
capability. To achieve enough instrument volume to justi-
fy the expenditure of development funds, the require-
ments for SVI and SVI have been merged
‘An essential next step is the solicitation of design/ price
responses from responsible instrument manufacturers
followed by a joint user/vendor review of the proposals
This joint review should be followed by the emergence of
instrument system specifications that will be incorporated
into the Pharmacopoeia (788) particulate quality mea:
surement requirements. An essential future action is the
establishment of a framework within which design asser-
tions can be objectively evaluated against performance to
avoid perpetuation of the present difficulties
Sample Processing Capability
‘Sample procesing capability should be a minimum of 100
mL/min for each input channel. The input channel should
be designed and tested to provide fully developed laminar
flow in the detector. The >100-mL /min volume process-
ing capability needed to eliminate container sampling for
the bulk of SVI requirements should be available through
use of a multiple input system with up to 5 input channels,
The multiple input channels will share microcomputer
control, analysis, and data output capability
318
‘System Capability
1 The sample handling sizing and counting efficiency of
the entire particulate analysis system should be in ex-
ess of 98% from 4 to 100 um for particle densities from
1.05 to 8.03 at the specified flow rate.
2, System resolution should be at least 5% for the smallest
particle size in the measurement range. A 128 channel
analysis capability is required for this extended range.
3. The sensor should be capable of analyzing 6500 parti-
cles/ mL with a maximum of 5% coincidence error.
4, Sample handling containers and agitators which are
compatible with the particle sensor should be provided.
The performance of these accessories should be certi-
fied to provide homogenous particulate input over the
entire range of particle sizes (4-100 zm) and densities
(1.05-8.03),
5. The system should have the capability to analyze and
display the (788) described maximum particle dimen-
sion for spheres, irregular shapes (ACFTD), flakes,
and fibers.
6. Thesystem should be capable of automated calibration
swith monodisperse spheres.
7. The system should be capable of 2.5% flow accuracy
and -£1% volume accuracy using a stepper motor sy-
ringe pump. Liquid pressure pulsations should be fil-
tered to 1% at all flow velocities required for particu-
late analysis.
8. The signal-to-noise ratio should be 100:1 for all mea-
surements from 10-100 um. At the 4-um lower mea-
surement limit the signal-to-noise ratio should be no
lower than 20:1
9. Isolation should be provided on power and signal input
lines to ensure that particle sizing and counting shall be
unaffected by electrical noise spikes.
System Maintenance
1. The system assembly should be modular with certified
mean time between failures of 2500 hours.
2. Remote diagnostic capability should be available to
facilitate user replacement of plug-in or bolt-on mod-
ules,
3. The sensor light source should be rated for either 3000-
hour life or be capable of user field replacement and
alignment without special tools or fixtures within a one
hour period
Journel of Parenteral Science & TechnologyPart II—A Selected Annotated
PATRICK P. DeLUCA*, BICE CONTI", and JULIUS Z. KNAPPt
jiography on Particulate Matter
* University of Kentucky, College of Pharmacy, Lexington, Kentucky. 1 University of Pavia, Pavia, Haly. Research & Development
Associates, Inc, Somerset, New Jersey
ABSTRACT: This selected Annotated Bibliography on Particulate Matter represents a summary of the
information obtained from a literature search on particulate matter. This information was necessary 10
develop an unbiased professional evaluation of the instrumentation now marketed for the analysis of
particulates in parenteral solutions. As such, special emphasis has been placed on instrument evaluations and
comparisons.
|. Particle Counting (Size Analysis)
A. General
1
Physics of particle size analys
3, (1954,
‘A compilation of papers on: a) a comparison of methods for
particle size analysis, b) scattering absorption of light, c) pho
twestnction measurements on spherical particles ) the signi
cance and application of shape factors, e) a particle profile est,
Strip for microscopesly assessing the accuracy of sizing iregu
larly shaped particles, fa survey of the automatic couating and
sizing methods, ) th theory of particle sizing and counting by
trace scanning, ) some fundamental aspects of particle count
ing and sing by ineseans,i the automatic size analysis of dust
‘deposits by means of an illumination sit, the automatic count-
ing of red blood cell, and ) testing a counting machine,
4) A comparison of methods for particle size analysis (p. 21)
‘An investigation af sedimentation methods of incremental iy,
to analyze particle sizes over range of 2-83 and 20.76 um
(Course dusts). The following table surnmarizes the methods;
Brit. J. Appl Phys. Suppl,
Particle
SizeRange, Concentration, Accuracy
Method um % &
Pipette nts 1 High
Hydrometcic 0-25 001 215
035 oor 225
Diver 0-25 O01 21
Root Diver 10-53 001 15
Manometric
‘Open 1s als
Closed 533 a3
Photoextinction® 1-25 = 46
Electrical
Resistance? 15-40 = -
= Measures optical density ofa suspension from which size
vejght analysis ean be made
‘Measurement ofthe change in resistance ata suitable sam
pling depth, gives a dust concentration curve
1) Scattering absorption of light by particles (p. 64). Survey of
theories about scattering and absorption of ight by particles,
Discussion of Mie theory and Mie effect for large and very small
particles (004 jim) using Raleigh scaitering, The seatcering
coefficient fluctuated with decreasing amplitude inthe diffrac-
tion region, The instrument was calibrated by measuring the
‘ross sectional area of particles using axial ight extinction, the
calibration was simpler for opaque particles than for transparent
particles,
Dr. Contihelda Post Doctoral Scholar appointment atthe University
of Kentucky,
"Astersked articles sre surnmarized
Vol, 42, Supplement 1988
Inthe Raleigh region the sensitivity of measuring smal pri
les in the presence of large ones wat increased by varying the
Screening coefficient with wavelength,
For Irum particles xrays were used as the illumination
6) Photoextinetion measurement on sphercol parties (p. 71)
Using incident radiation a total seatering coefficient iealelat-
co sing the folowing equation,
he
tog “2 optical density (&q.)
‘optical density = K log e"*7 (Eq.2)
isthe otal scaterng ooefcient and canbe calculated wsing
tithe the theories of Mie or Vandetulst. It depends onthe ato,
ofthe radius of particles, rand the wavelength ofthe radiation
{5 well asthe reactive index ofthe parle relative to the
Surrounding medium, Examples are given using Barium sulfite
and Lyeopodium pyriforme spores.
4) The significance and application of shape factors in particle
Size anatyts (5.82). By Ineasuring the thickness of individual
fubseve particles with the optiea! microscope and the dimen-
sions of the projected images, surface and volume shape factors
‘were calculated. An expression was derived for the ratio of the
particles projecte diameter tots Stokes’ ameter.
‘A large variation inthe shape facors between particles wes
foand for col dust and for particles of sme other materials
“The largest partis of ssubsive fraction ofa powder have
shape factors different fom those ofthe smaller sizes.
©) A particle profile test srip for assessing the accuracy of
Siving regularly shaped particles with microscope (p. 105)
‘A patil profile test strip thal can be viewed microscopically
Bives a realistic impresion of black dust and « quantitative
estimation of observer bias. Tecan be used Tor assessing the
rors of sizing irregularly shaped particles, using a globe and
citcleeyepicegraticule
f) Surcey ofthe automatic counting and sizing of particles (p
121): Presents the principles on which some automatic counting
devices are based. Particles were counted by seaming two spots
Problems encountered included randomness ofthe sample coin.
cidence and counting very small prices.
8) Theory of particle sing and counting by tack scanting (p.
125), A microscopic method using» photoelectric detecting
system with high speod pulses allowed forthe measurement of
projected area, Problems encountered included the counting nd
Sizing of nonspherical parle, coieidence, and over.
1) Some fundamental axpects of particle counting and sizing
2by line soon (p. 133). A method of using line seans (0 size
articles which approach the limit of optical resolution as
eseribe,
‘Scanning by spot—Use ofa simple on-off detector
Scanning by spots—Use ofa simple on-off detector
Scanning by sit—Use of simple on-off detector
By relating derivable information to observed daa of frequency
interception of patiles by lines scans and combination of ines
Scans ood accuracy was reported.
S191) The automatic size analysis of dust deposits by means of an
Ittwmization slit (p. 143). A encroscopte comparison of the
‘rious methods for automatic counting and sie analysis of
Sample produet pulverized to microscope sizes using photogra-
‘py. The principle was to detect and count diserte light im-
pulses using a photocell. Erors were attributed to fractional
fotcteeption of particles. overlap coincidence, and very small
particles. Statistical solutions to these problems were described,
More precise size distributions were reported Oy Wsing (wo
images at diffecent magnifications. An apparatus based on sut-
face area determination was described
5) The automatic counting of red blood cells (P- 147). An
Apparatus in which the blood cells are scanned by mecha
‘oscillation ofa microscope stage was described. The novel shape
ofthe scanning aperture was found to influence the errors ars
ing from various sources. The results in counting blood cells were
reported reproducible within 3%.
i) Testing @ counting machine (p. 161). Particle sizing and
counting machin results are compared withthe results obtained
‘when sizing with 2 microscope. A machine which measures the
size frequency distribution of chords oblained from moving
siains obtained by spraying a black dye at uniform velocity in
Front of alight sensitive detector was compared withthe miero-
‘cope. From the total numberof chords in each of several ranges
it tae posible to compute the approximate number of circular
stains from which they were derived. The counting machine
measured quickly, with an accuracy better than 1% ofthe range
‘which was felt tobe lower than that associated with eye count
ing
Groves, M.J.""The size distribution of particles contaminating
parenteral solutions,” Analyst, 94, 992 (1969).
‘One of the earlier studies in which the log-log distebtion was
tested. Forty-five samples of injection BP from
and it wos dificult ocorelate microscope and Coulter Count
for particles <15 jim. Te was almost imposibie 1 distinguish
small particles with refractive index similar tothe membrane
jon within a batch was noted. To avoid the effect of
‘vacation within a batch an index of cleanliness was sugeested
3. Apt, B:K.."Pariculate matter in intravenous infusions, East.
Pharm. 15(176), 27-31 (1972)
4. Emnert, ., "Studies on the problem of particulate mater in
parenteral products,” Sten. Farm. Tidskr, 78, 129-139 (Feb,
1973).
5. Akers, R. J, Lyd, P. J. and Scares, B. “European Sympo-
‘ium on particle size measurement." DECHEMA-Monogr., 79,
Pat 8, 191-208 (1973),
This was a review of the history of automatic microscope
Particle size analysis systems, The semiautomated Zeiss-Endter
particle size apparatus was described in which ercles are super-
Imposed o macroscopic images. It was reported to be relatively
fee of erors. An automatic microscopic technique using a Leitz
CClassimat, Zeiss Videomat was deseribe. This involved genera
tion ofa Fectangulr rater formed by progressively moving &
scanning soto” sit over the image and was reported 10 be quite
Stitable fr routine measurement.
‘A digital computer particle size analysis system was the
‘Quantimet 720 scanner system with & high quality vidicon or
plumbioon camera system capable of resolving afield of 880 x
{S88 picture points with high sabity, This ublized TTL digital
logic circuitry and a FORTRAN subroutine to evaluate particle
parameters,
The disadvantages of automatic image processing systems
were reported. These included inability to sole problem of
{ouching and overlapping particles of arbieary shape. A
‘pen was used to identi specitic images
6, Davis, PJ. Dasley, R. W. and Patel, N.. "Particulate contami:
ration in parenteral solutions.” (Procesdings) J. Pharm. Phar
‘macol. 31, Suppl. 59P (Dec. 1979)
7. Longe, &. 1, "Particulate contamination in selected parenteral
frogs,” Can. Anaesth, Soe. J, 21(1), 62 4, (1980).
. Andrews, D.. "Particulate contamination in thiopental solu
sions." Can. J. Hosp. Pharm. 31031). 3 (1988),
‘Seealso Reference 67
B. Large Volume Solutions
9, Lines. R. W., “Counting of particulate matter in parenteral
solutions: 1. Survey of the literature,” Bull. Parenter. Drug’
Assoc. 244). 113-17 (Review) (1967),
Davis.N. M. Tureo,S..andSivelly EA study of particu
‘matter in iy. infusion fluids.” mt. J. Hosp. Pharm. 21, 82
826 (Oat. 1970),
Darby, TD, aad Ausman, RK. “Particulate matter in polyi-
nyt chloride intravenous bags (Cont.),” NEW. Med. 290, 579
(1975).
Hayashi, T. “Occurrence and size distribution of
maiter in parenteral solutions,” Yakuzaigaku 40,
(Galy 15,1980), Japanese
“Messerschmidt, W.. "Particulate contamination in infusion so-
lutions,” Krankenhauspharmazie 1, 2), 24-26 (Oct. 1980),
German.
Caramella, C., Montanari, L, Pavanetto, F. and Ponci, R
“Research on particle contamination of injectable solutions.”
Farmaco, Ed. Prat. 36, 148-16| (Mar. 1981), lalian,
'A comparison of the Coulter Counter with mierascope using
35 commercial solutions, Al solutions met the USP LVP limits,
‘while only 9 complied with British Pharmacopoeia mis, Using
microspheres asa ealibrant no difference was found between the
‘microscopic and Coulter Counter methods. With ACFTD as a
calibrant, differences of 25% were found atthe 10am size: the
iference increased with increasing size of paris. I was.
concluded that the Coulter Counter should be limited to 10-am
size partes.
Broussali-Tsiftsoglou, T.. and Iconomeu-Petrovitch, N. G.,
"Methods for detection and quantitative determination of par-
‘cule matier in parenteral solutions,” Pharm, Delt. Epistem.
Ekdosis,8(1), 73-89 (1982).
Budgen, C.J, and Frost, L, "Reuse of glass containers for
Irrigation solutions.” N.2. Pharm. 3:1) 45-46 (1983).
“Montanari L. Pavanetto,F and Pon, R. “Investigation of
foceign particle contamination in high volume injectable so}
tions and in powders for injectable solutions. Proposals for Ital-
Tan reolatons" Farmaco Ed. Pra37,397-407 (De. 1983),
alin
‘Sixteen LP batches from twelve manufacturers end ten dry
powders from nine manufactures were studied using the Cou
ter Counter. Eleven of the sixteen LVPs passed USP limits,
while four ofthe sixteen passed the British Pharmacopeia.
Besedina, 1. V."Conductometrie method for determination of
the range of particle dimensions in injection solutions,” Farmat-
siya (Moscow) 33(1), 30-22 (1988), Russian
Maines-Nutt, RF ané Muaton, T-1., "Particle size measure:
ment in intravenous Nui.” J, Pharm. Pharmacol, 36(8),534—
6 (1984).
Lage varacons were observed ina comparison ofthe HIAC
and Coulter Counter for monitoring LVPS. Since variations
‘ould not be explained on bass of shape factors, it was coneluded
the correlation ofthe twe methods was not posible
Coulter counts were an order of magnitude higher at am and
from 016 to 5X at 5 gem. The differences between HIAC and
Coulter were not comparable with salt and sugar slutions. For
small particles, the HIAC was found to count les than the
Coulter due to forward scattering For particles with refractive
index close tothe solution, the HLAC again counted les.
Meserschmidt, W., "Extent and accepiable limits of partion:
late matter in infusion solutions,” Krenkenhauspharmaste, 5,
277-282 (Sep, 1984), German,
See lso References, 64, 90.and 98,
C. Small Volume Solutions
a
2.
2.
Lines, R. W., “Counting of particulate matier in parenteral
solutions” I. Partcie counting in small containers.” Bull. Par-
enter Drag Assoc, 21(8), 118-123 (1967).
‘One of the early studies on particles using the Coulter
‘Counter. Good reproducibility was found in the various solations
studied. Handling and sampling were more eritcal with small
‘volume parenteral.
Dungan, D. J, “Particulate contamination in pharmaceutical
preparations for injection,” Aust. J. Pharm. 40,($84),S59-S64
(Aug. 1968),
Somerville, T.G., and Gibson, M., “Particulate contamination
‘inampuls," Pharm. J. 211, 128-130 (Aug. 18 1973)
‘This was a comparative analysis of S0-am particles ia am-
poules using a Polarized light viewer (Allen type 208/2) and a
‘Coulter Counter (Medel T, 70:gm orifice). Both techniques
showed a spread of eadings but sherewasa reported comparison
Journal of Parenteral Science & Technology