10 CSR 10-5.442
Control of Emissions From Lithographic and Letterpress
Printing Operations
PURPOSE: This rule restricts volatile organic compound emissions from lithographic and
letterpress printing operations in the St.
Louis 1997 eight (8)-hour ozone nonattainment area.
PUBLISHER’S NOTE: The secretary of state
has determined that the publication of the
entire text of the material which is incorporated by reference as a portion of this rule
would be unduly cumbersome or expensive.
This material as incorporated by reference in
this rule shall be maintained by the agency at
its headquarters and shall be made available
to the public for inspection and copying at no
more than the actual cost of reproduction.
This note applies only to the reference material. The entire text of the rule is printed
here.
(1) Applicability.
(A) This rule applies to installations that
operate offset lithographic printing presses,
letterpress printing presses, or both, including heatset web, non-heatset web (newspaper
and non-newspaper), and non-heatset sheetfed presses in St. Louis City and Jefferson,
St. Charles, Franklin, and St. Louis Counties
existing on August 30, 2011.
(B) This rule applies only to installations
described in subsection (1)(A) of this rule,
with total actual emissions from lithographic
and letterpress printing operations, including
related cleaning activities, before consideration of controls, of more than three (3) tons
per twelve (12)-month rolling period of
volatile organic compounds (VOCs).
(C) This rule does not apply to printing on
fabric, metal, or plastic.
(D) Once the installation exceeds the
applicability level of this rule, it shall remain
subject to this rule even if its actual emissions
drop below the applicability level of this rule
until it can demonstrate, to the satisfaction of
the director, that the total actual VOC emissions from lithographic and letterpress printing operations including related cleaning
activities, before consideration of controls, is
less than three (3) tons per twelve (12)-month
rolling period for sixty (60) consecutive
months.
(E) VOC emissions calculations guidance
may be found in subsection (5)(D) of this
rule. As an alternative, the material use guidance in subsection (5)(E) of this rule may be
used to determine applicability.
(2) Definitions.
(A) Alcohol—Refers to isopropanol, isopropyl alcohol, normal propyl alcohol, or
ethanol.
(B) Alcohol substitutes—Nonalcohol additives that contain volatile organic compounds
and are used in fountain solution.
(C) Automatic blanket wash system—
Equipment used to clean lithographic blankets which can include, but is not limited to,
those utilizing a cloth and expandable bladder, brush, spray, or impregnated cloth system.
(D) Cleaning solution—A liquid solvent
used to remove printing ink and debris from
the surfaces of the printing press and its
parts. Cleaning solutions include, but are not
limited to, blanket wash, roller wash, metering roller cleaner, plate cleaner, impression
cylinder washes, and rubber rejuvenators.
(E) Fountain solution—The solution which
is applied to the image plate to maintain the
hydrophilic properties of the nonimage areas.
It is primarily water containing an etchant, a
gum arabic, and a dampening aid (commonly
containing alcohol and alcohol substitutes).
(F) Fountain solution reservoir—The collection tank that accepts fountain solution
recirculated from printing unit(s). In some
cases, the tanks are equipped with cooling
coils for refrigeration of the fountain solution.
(G) Heatset—A class of web-offset lithographic and letterpress printing in which the
setting of the printing inks requires a heated
dryer to evaporate the ink oils. The setting or
curing of inks using only radiation (e.g.,
infrared, ultraviolet light, or electron beam)
is not heatset and is classified as nonheatset.
(H) Letterpress printing—A printing process in which the image area is raised relative
to the nonimage area, and the ink is transferred to the substrate directly from the image
surface.
(I) Lithographic printing—A planographic
printing process where the image and nonimage areas are chemically differentiated; the
image area is oil receptive and the nonimage
area is water receptive. This method differs
from other printing methods, where the
image is typically printed from a raised or
recessed surface. Offset lithographic printing
is the only common type of lithographic
printing used for commercial printing.
(J) Offset lithographic printing—A printing
process that transfers the ink film from the
lithographic plate to an intermediary surface
(rubber-covered blanket cylinder), which, in
turn, transfers the ink film to the substrate.
(K) Press—A printing production assembly
that can be made up of one (1) or many units
to produce a finished product. This includes
any associated coating, spray powder application, heatset web dryer, ultraviolet or electron
beam curing units, or infrared heating units.
(L) Printing—Any operation that imparts
color, images, or text onto a substrate using
printing inks.
Specific to the St. Louis Metropolitan Area
(M) Printing ink—Any fluid or viscous
composition used in printing, impressing, or
transferring an image onto a substrate.
Varnishes and coatings applied with offset
lithographic and letterpress printing presses
are inks and are part of the applicable printing process, not a separate operation such as
paper coating.
(N) Sheet-fed—A printing press where
individual sheets of substrate are fed into the
press sequentially.
(O) Web—A printing process where a continuous roll of substrate is fed into the press.
(P) Definitions of certain terms in this
rule, other than those specified in this rule
section, may be found in 10 CSR 10-6.020.
(3) General Provisions.
(A) Fountain Solutions. This subsection
applies only to offset lithographic presses
with a total fountain solution reservoir capacity of one (1) gallon or more.
1. No owner or operator shall use or
permit the use of any applicable offset lithographic printing press unless—
A. For each heatset web press—
(I) The fountain solution, as
applied, contains one and six-tenths percent
(1.6%) or less by weight of alcohol; or
(II) The fountain solution, as
applied, contains three percent (3.0%) or less
by weight of alcohol and is refrigerated to a
temperature of sixty degrees Fahrenheit (60
oF) or less; or
(III) The fountain solution, as
applied, contains five percent (5.0%) or less
by weight of alcohol substitutes; and
(IV) The fountain solution mixing
tanks are covered for alcohol-based solutions;
B. For each sheet-fed press with a
maximum sheet size greater than eleven inches by seventeen inches (11" × 17")—
(I) The fountain solution, as
applied, contains five percent (5.0%) or less
by weight of alcohol; or
(II) The fountain solution, as
applied, contains eight and five-tenths percent (8.5%) or less by weight of alcohol and
is refrigerated to a temperature of sixty
degrees Fahrenheit (60 oF) or less; or
(III) The fountain solution, as
applied, contains five percent (5.0%) or less
by weight of alcohol substitutes or a combination of alcohol and alcohol substitutes; and
(IV) The fountain solution mixing
tanks containing alcohol-based solutions are
covered; and
C. For each non-heatset web press,
the fountain solution, as applied, contains no
alcohol and five percent (5.0%) or less by
weight of alcohol substitutes.
2. Direct measurement of the alcohol
content of the fountain solution, as applied,
shall be performed and recorded with a
hydrometer, equipped with temperature correction or with readings adjusted for temperature, at least once per day or once per batch,
whichever is longer. A standard solution shall
be used to calibrate the hydrometer once per
month for the type of alcohol used in the
fountain.
3. For fountain solutions, as applied,
containing alcohol substitutes or nonalcohol
additives and, as an alternative to paragraph
(3)(A)2. of this rule, the VOC content shall
be established with proper record keeping
which may include, as necessary to determine
compliance, the amount of concentrated substitute added per quantity of fountain water,
date of preparation, calculated VOC content
of the final solution, or by measurement
using 40 CFR 60, Appendix A, Method 24,
as specified in 10 CSR 10-6.030(22) analysis
as outlined in paragraph (5)(C)1. of this rule.
For automatic mixing systems, verification
and record keeping of the mixer settings shall
be performed at least once each month.
4. The fountain solution temperature for
each refrigerated fountain reservoir containing alcohol-based solutions shall be measured
at least once per day or once per batch,
whichever is longer, by a thermometer or
other temperature detection device capable of
reading to one-half degree Fahrenheit (0.5
oF).
(B) Press Cleaning. No owner or operator
shall use or permit the use of any applicable
offset lithographic or letterpress printing
press unless—
1. All cleaning solutions, excluding a
quantity not to exceed one hundred ten (110)
gallons per facility in any twelve (12) consecutive months, shall have a VOC content of
seventy percent (70%) or less, by weight, or
a composite partial vapor pressure less than
or equal to ten (10) millimeters of mercury
(Hg) at twenty degrees Celsius (20 oC);
2. The cleaning solutions are kept in
tightly-covered containers at all times except
when being dispensed as needed for cleaning
operations;
3. The used cleaning cloths contaminated with cleaning solutions are placed in tightly-closed containers while awaiting off-site
transportation. The cleaning cloths should be
properly cleaned and disposed; and
4. The VOC content or composite partial vapor pressure of the cleaning solution, as
applied, shall be established with proper
record keeping which may include, as necessary to determine compliance, the amount of
concentrated cleaning solution added per
quantity of water, date of preparation, calculated VOC content, composite partial vapor
pressure of the final solution, by measurement using 40 CFR 60, Appendix A, Method
24, as specified in 10 CSR 10-6.030(22)
analysis as outlined in paragraph (5)(C)2. of
this rule, or the formula in paragraph
(5)(C)3. of this rule. For automatic blanket
wash systems, verification and record keeping
of the mixer settings shall be performed at
least once each month.
(C) Heatset Web Press Emission Control
Systems. This subsection applies only to
heatset web lithographic and letterpress printing presses with the potential to emit (PTE)
VOCs from ink oil greater than twenty-five
tons per year (25 tpy) unless any such press
is used for book printing or has a maximum
web width of twenty-two inches (22") or less.
1. No owner or operator shall use or
permit the use of any press without a dryer
which has one hundred percent (100%) of its
exhaust ducted to a control device that is
maintained and operated to achieve, at all
times while the press is operating, at least the
indicated percentage by weight control efficiency.
The dryer pressure shall be maintained below
the pressure of the press room at all times
while the press is operating. Continuous
dryer air flow monitoring is not required.
2. As an alternative to achieving the
applicable control efficiency in paragraph
(3)(C)1. of this rule, any press shall operate
its control device to maintain a maximum
VOC outlet concentration of twenty parts per
million by volume (20 ppmv) as hexane
(C6H14) on a dry basis.
(D) Use of emission control equipment
under subsection (3)(C) of this rule requires
that continuous temperature monitors be
installed, calibrated, maintained, and operated at all times while a connected printing
press is operating. Temperatures shall be
measured with an accuracy of plus or minus
seventy-five hundredths of one percent
(±0.75%) measured in degrees Celsius, or
two and one-half degrees Celsius (2.5 oC).
The operating temperatures to be used as the
parameters for demonstrating continuous
compliance shall be determined per subsection (5)(A) of this rule. The monitors continuously shall measure—
1. For catalytic oxidizers, the gas temperature upstream of the catalyst bed;
2. For thermal and regenerative oxidizers, the oxidizer operating temperature; and
3. Any other parameters considered necessary by the director to verify compliance
and proper operation of emission control
equipment.
(4) Reporting and Record Keeping.
(A) All persons subject to this rule shall
maintain records as required by this section
sufficient to determine continuous compliance with this rule. These records shall be
kept for at least five (5) years, or longer if
enforcement action is pending, and made
available immediately upon request for
review by the Department of Natural
Resources’ personnel and other air pollution
control agencies upon presentation of proper
credentials.
(B) All persons subject to subsection
(3)(C) of this rule shall maintain records for
each control device sufficient to demonstrate
that the control efficiency is being maintained. These records shall include, but are
not limited to:
1. The temperature readings, logged at
least once every fifteen (15) minutes, from
the monitors required by paragraphs (3)(D)1.
and (3)(D)2. of this rule; and
2. The operating parameters of any
required control device determined from any
initial or subsequent control efficiency compliance testing as outlined in subsection
(5)(A) of this rule.
(C) For each applicable printing press,
records shall be maintained to show—
1. For each fountain solution whose
VOC content is modified, the calculation or
direct measurement data that indicates the
resultant VOC content by weight. The calculation or measurement need only be performed once for each batch of fountain solution used except that it need not be performed
at all for the dilution of a fountain solution
containing alcohol substitutes purchased with
less than five percent (5.0%) VOC content
before dilution or for alcohol containing
fountain solutions requiring refrigeration purchased with less than three percent (3%) or
eight and five tenths percent (8.5%) VOC
content, for heatset web and sheet-fed presses, respectively;
2. For each fountain solution, a manufacturer’s formulation data sheet or Material
Safety Data Sheet (MSDS) listing the physical properties of alcohol or alcohol substitute(s) such as density and percent VOC as
purchased from the supplier;
3. Results of any testing conducted on an
emission unit at a regulated facility;
4. Maintenance records and inspection
results of any air pollution control equipment; and
5. The temperature, as required by paragraph (3)(A)1. of this rule, at least once per
day or once per batch, whichever is longer.
(D) For each lithographic and letterpress
printing installation subject to this rule,
records shall be maintained to show—
1. A Material Safety Data Sheet or manufacturer’s formulations data listing the percentage by weight of VOC in the cleaning
solution, the composite partial vapor pressure
of VOC in the cleaning solution, or the necessary data to make a determination thereof
as outlined in subsection (5)(C) of this rule;
2. For each cleaning solution whose
VOC content is modified, the calculation that
indicates the resultant VOC content by weight
or composite partial vapor pressure. The calculation need only be performed once for
each batch of cleaning solution used except
that it need not be performed at all for the
dilution of a cleaning solution which does not
exceed the VOC limits of paragraph (3)(B)1.
of this rule; and
3. The quantity of all cleaning solution
used which does not meet the VOC limits set
forth in paragraph (3)(B)1. of this rule on a
twelve (12)-consecutive-month basis.
(E) The director may require other records
as reasonable and necessary to carry out the
provisions of the Missouri Air Conservation
Law.
(5) Test Methods. Certain test methods mentioned in this rule may be found in 10 CSR
10-6.030.
Other
U.S.
Environmental
Protection Agency test methods specific to
this rule may be found in 40 CFR 60,
Appendix A as specified in 10 CSR 106.030(22).
(A) Control Efficiency Testing. To demonstrate compliance with the emission limits of
subsection (3)(C) of this rule, an initial emission test shall be performed after any
required control equipment is installed. The
emission limits are not met until compliance
has been verified through this testing. Testing
is also required within one hundred eighty
(180) days after significant modifications to
any control equipment required by this rule.
Significant modifications include any repairs
or changes that might substantially alter or
affect the overall control efficiency. This subsection outlines the methods to be used for
any such testing.
1. The emission unit shall be run at typical operating conditions and flow rates compatible with scheduled production during any
emission testing.
2. Capture efficiency testing for heatset
dryers is not required if it is demonstrated
that pressure in the dryer is negative relative
to the surrounding press room and the airflow
is into the dryer. This test may be performed
with a differential pressure gauge or an airflow direction indicator (e.g., smoke stick or
aluminum ribbons).
3. EPA Method 1 or 1A, as specified in
10 CSR 10-6.030(22), as appropriate, shall
be used to select the sampling sites.
4. EPA Method 2, 2A, 2C, or 2D, as
specified in 10 CSR 10-6.030(22), as appropriate, shall be used to determine the velocity
and volumetric flow rate of the exhaust
stream.
5. EPA Method 3 or 3A, as specified in
10 CSR 10-6.030(22), as appropriate, shall
be used to determine the concentration of
oxygen (O2) and carbon dioxide (CO2).
6. EPA Method 4, as specified in 10
CSR 10-6.030(22), shall be used to determine moisture content.
7. EPA Method 25, 18, or 25A, as specified in 10 CSR 10-6.030(22), shall be used
to determine the VOC concentration of the
exhaust stream entering and exiting the control device, unless the alternate limit in paragraph (3)(C)2. of this rule is being used for
compliance, in which case only the VOC concentration of the exit exhaust shall be determined. In cases where the anticipated outlet
VOC concentration of the control device is
less than fifty (50) ppmv as carbon, EPA
Method 25A, as specified in 10 CSR 106.030(22), shall be used.
8. If EPA Method 25A, as specified in
10 CSR 10-6.030(22), is used—
A. The outlet readings from a thermal
or catalytic oxidizer may be corrected by
using EPA Method 18 or 25, as specified in
10 CSR 10-6.030(22), to determine non-VOC
components (methane and ethane) and subtracting these from the Method 25A result;
and
B. The director may require a retest
by EPA Method 18 or 25, as specified in 10
CSR 10-6.030(22), if the average corrected
outlet reading is greater than fifty (50) ppmv
VOC as carbon.
9. A compliance test shall consist of up
to three (3) separate runs, each lasting a minimum of sixty (60) minutes unless the director determines that the circumstances dictate
shorter sampling times.
10. EPA Method 25, as specified in 10
CSR 10-6.030(22), specifies a minimum
probe temperature of two hundred sixty-five
degrees Fahrenheit (265 °F). To prevent condensation, the probe should be heated to at
least the gas stream temperature, typically
close to three hundred fifty degrees
Fahrenheit (350 °F).
11. EPA Method 25A, as specified in 10
CSR 10-6.030(22), specifies a minimum
temperature of two hundred twenty degrees
Fahrenheit (220 °F) for the sampling components leading to the analyzer. To prevent condensation when testing heatset printing presses, the sampling components and flame ionization detector lock should be heated to at
least the gas stream temperature, typically
close to three hundred fifty degrees
Fahrenheit (350 °F).
12. The oxidizer operating temperature
or the temperature of the gas upstream of the
catalyst bed may be used as the operating
parameter for determining continuous compliance with the emission standard of subsection
Specific to the St. Louis Metropolitan Area
(3)(C) of this rule. This temperature shall be
computed as the time-weighted average of the
temperature values recorded during the test.
The owner or operator must maintain the oxidizer at a three (3)-hour average temperature
equal to or greater than a temperature fifty
degrees Fahrenheit (50 °F) below the average
temperature observed during the most recent
stack test to demonstrate continuous compliance.
13. Use of an adaptation to any of the
methods specified in this subsection may be
approved by the director on a case-by-case
basis. The owner or operator shall submit
sufficient documentation for the director to
find that the methods specified in this subsection will yield inaccurate results and that the
proposed adaptation is appropriate.
(B) Control Device Inspection. For catalytic oxidizers, the catalyst bed material shall be
inspected annually for general catalyst condition and any signs of potential catalyst depletion. The owner or operator shall also collect
a representative sample of the catalyst from
the oxidizer, per manufacturer’s recommendations, and have it tested to evaluate the catalyst’s capability to continue to function at or
above the required control efficiency. An
evaluation of the catalyst bed material shall
be conducted whenever the results of the
inspection indicate signs of potential catalyst
depletion or poor catalyst condition based on
manufacturer’s recommendations, but not
less than once per year.
(C) VOC Content Testing.
1. Fountain solutions. Compliance with
the VOC content limits for fountain solutions
established in subsection (3)(A) of this rule
shall be determined by one (1) of the following:
A. If fountain solution is diluted prior
to use, a calculation that combines EPA
Method 24, as specified in 10 CSR 106.030(22), analytical data for the concentrated materials used to prepare the fountain
solution and the proportions in which they
are mixed to make the as-applied material.
The analysis of the concentrated materials
may be performed by the supplier of those
materials. Owners or operators may use formulation information provided with the concentrated materials used to prepare the fountain solution, such as the container label, the
product data sheet, or the MSDS sheet to
document the VOC content of the concentrated material;
B. If fountain solution is not diluted
prior to use, MSDS or manufacturer’s formulation data sheet may be used; or
C. EPA Method 24, as specified in 10
CSR 10-6.030(22), of a sample of fountain
solution, as applied.
2. Cleaning solutions. The VOC content
or VOC composite partial vapor pressure of
cleaning solutions shall be determined by one
(1) of the following:
A. Analysis by EPA Method 24, as
specified in 10 CSR 10-6.030(22), for VOC
content or by an appropriate method for VOC
composite partial vapor pressure of a sample
of the cleaning solution. See formula in paragraph (5)(C)3. of this rule. The analysis may
be performed by the supplier of those materials; or
B. Calculation for VOC content that
combines EPA Method 24, as specified in 10
CSR 10-6.030(22), analytical data for the
concentrated materials used to prepare the
cleaning solution and the proportions in
which they are mixed to make the cleaning
solution as applied. Owners or operators may
use formulation information provided with
the concentrated materials used to prepare the
cleaning solution, such as the container label,
the product data sheet, or the MSDS sheet to
document the VOC content of the concentrated material;
C. If cleaning solution is not diluted
prior to use, MSDS or manufacturer’s formulation data sheet may be used.
3. Calculations. The VOC composite
partial vapor pressure is the sum of the partial
pressure of the compounds defined as VOCs.
VOC composite partial vapor pressure is calculated as follows:
n (Wi)(VPi)/MWi
PPc = å Ww + Wc + n Wi
i=1MWw MWc
å MWi
i=1
Where:
Wi = Weight of the ith VOC com-
pound, in grams
Ww = Weight of water, in grams
Wc = Weight of exempt compound,
in grams
MWi = Molecular weight of the ith
VOC compound, in g/g-mole
MWw = Molecular weight of water, in
g/g-mole
MWc = Molecular weight of exempt
compound, in g/g-mole
n = Number of VOC compounds
PPc = VOC composite partial vapor
pressure at 20 °C (68 °F), in
mmHg
VPi = Vapor pressure of the ith VOC
compound at 20 °C (68 °F),
in mmHg
(D) VOC Emission Calculations, Retention
Factors, and Capture Efficiencies. For purposes of determining VOC emissions from
lithographic and letterpress printing operations, the following retention factors and capture efficiencies and formula shall be used:
1. A portion of the VOC contained in
inks and cleaning solution is retained in the
printed web or in the shop towels used for
cleaning. The following retention factors
shall be used:
A. For heatset inks printed on absorptive substrates, a twenty percent (20%) VOC
retention factor shall be used meaning eighty
percent (80%) of the VOC in the ink is emitted during the printing process and is available for capture and control by an add-on pollution control device;
B. For sheet-fed and non-heatset web
inks printed on absorptive substrates, a ninety-five percent (95%) VOC retention factor
shall be used, meaning five percent (5%) of
the VOC in the ink is emitted during the
printing process; and
C. For cleaning solution VOC emissions from shop towels using cleaning solutions with a VOC composite vapor pressure
of no more than ten (10) mmHg at twenty
degrees Celsius (20 °C) (sixty-eight degrees
Fahrenheit (68 °F)), a fifty percent (50%)
VOC retention factor shall be used if the contaminated shop towels are kept in closed containers;
2. A portion of the VOC contained in
inks, fountain solutions, and automatic blanket washes on heatset presses is captured in
the press dryer for control by add-on pollution control devices. The following capture
factors shall be used:
A. For inks, a one hundred percent
(100%) VOC capture efficiency shall be
used. All the VOC in the ink that is not
retained is assumed to be volatilized in the
press dryer if it is demonstrated that the pressure in the dryer is negative relative to the
surrounding press room and the airflow is
into the dryer;
B. For fountain solutions containing
alcohol substitutes, a seventy percent (70%)
VOC capture factor shall be used; and
C. For automatic blanket wash solutions with a VOC composite partial vapor
pressure of no more than ten (10) mmHg at
twenty degrees Celsius (20 °C) (sixty-eight
degrees Fahrenheit (68 °F)), a forty percent
(40%) VOC capture factor shall be used; and
3. For calculating VOC emissions, the
following equations shall be used:
A. For total VOC emissions from an
offset lithographic printing facility, including
all related cleaning activities—
Where:
VOCTOT = Total VOC emissions,
expressed as pounds
WINK = Weight of ink used,
expressed as pounds
VOCINK = Weight fraction of VOC in
the ink
RFINK = Retention factor of the ink,
expressed as a percent
m = Number of inks
VOLFS = Volume of fountain solution
used, expressed as gallons
VOCFS = VOC content of fountain
solution, expressed as
pounds per gallon
n = Number of fountain solu-
tions
VOLCS = Volume of cleaning solution
used, expressed as gallons
VOCCS = VOC content of cleaning
solution, expressed as
pounds per gallon
RFCS = Retention factor of the
cleaning solution, expressed
as a percent
p = Number of cleaning solu-
tions
and
B. For VOC ink oil emissions from a
heatset web lithographic or letterpress printing press—
n
VOCTOT = å WINKi * VOCINKi * (1− RFINKi)
i=1 100
Where:
VOCTOT = Total VOC emissions,
expressed as pounds
WINK = Weight of ink used,
expressed as pounds
VOCINK = Weight fraction of VOC in
the ink
RFINK = Retention factor of the ink,
expressed as a per-
cent
n = Number of inks
(E) Material Use Guidance: Applicability
Determination. Based on EPA’s Potential to
Emit (PTE) Guidance for Specific Source
Categories (April 14, 1998), and the equations of paragraph (5)(D)3. of this rule, the
methods in this subsection may be used for
determining if a facility or press meets the
corresponding applicability thresholds.
1. For determining if a facility meets the
applicability limits of subsection (1)(B) of
this rule, the material use thresholds are as
follows:
2. For determining if a web heatset press
is subject to subsection (3)(C) of this rule, the
material use thresholds are as follows:
AUTHORITY: section 643.050, RSMo 2016.*
Original rule filed Oct. 7, 1994, effective
May 28, 1995. Amended: Filed Nov. 30,
2010, effective Aug. 30, 2011. Amended:
Filed March 20, 2019, effective Jan. 30,
2020.
*Original authority: 643.050, RSMo 1965, amended
1972, 1992, 1993, 1995, 2011; transferred from 203.050
in 1986.