Question: What are the typical scrap rates for injection molding operations? Please provide specific percentages for different materials, machine types, or process conditions.

INJECTION MOLDING SCRAP REDUCTION: A STUDY IN
THE RELATIONSHIPS OF PLASTICS PROCESSING METHODS
By
Duoc T. Nguyen
A Research Paper
Submitted in Partial Fulfillment of the
Requirements for the
Master of Science Degree in
Management Technology
Approved for Completion of 3 Semester Credits
INMGT 735
Research Advisors
The Graduate College
University of Wisconsin
May 2004
The Graduate School
University of Wisconsin - Stout
Menomonie, WI 54751
ABSTRACT
Nguyen
(Writer)
(Title)
(Last Name)
Injection Molding Scrap Reduction: a Study in the
Relationships of Plastics Processing Methods
Duoc
(First)
T.
(Initial)
Management Technology Robert H. Feirn & Linards Stradins
57 Pages
(Graduate Major)
(Research Advisor) (Month/Year) (No. of Pages)
5/2004
Publication Manual of the American Psychological Association
(Name of Style Manual Used in this Study)
To maintain competitiveness and maximize profits in today's marketplace, one of
the most important aspects that organizations must focus on is scrap reduction. In the
plastics industry Phillips Plastics-Short Run, an injection molding facility, methodically
collects data in an effort to better understand and control scrap generation.
The purpose of this research is to analyze the scrap levels associated with
variances occurring in the injection molding machines, processes, materials, and
operators at the Short Run facility. The results help to identify the possible causes of
scrap and will lead to an appropriate solution to support Short Run in reducing scrap.
Acknowledgements
Thanks to John Ahlbrecht, Pete Posch, and Matt Rominski, the Plant Manager,
Production Manager, and Maintenance Manager, respectively, at Phillips Plastics-Short
Run in directing and supporting the data collection for this research.
Thanks to Mike Cran, Linda Whitcome, and Ron Watrud, 1st, 2nd, and 3rd shift
Supervisors at Short Run for supporting the collection of the necessary data related with
operators and their years of experience.
Thanks to Mr. Robert H. Feirn and Mr. Linards Stradins, my dedicated advisors,
for all their patience and knowledge to assist me through careful reading and support
through valuable feedback to edit this paper.
Particular thanks go to Mr. James Keyes, my wonderful teacher at UW-Stout in
Management Technology in putting his time in reviewing the research and giving me the
great comments and feedback to improve the text of this research.
Finally, special thanks to my wife, my daughter, and my son whose care and
encouragement lifted me over a tough spot.
Table of Contents
Abstract..
Chapter 1.
Introduction..
Statement of Problems
Objectives of the Study.
Purpose.........
Limitations.
Definitions...
Chapter 2..........
Literature Review.
Introduction.....
Machine......
Process
Material.
Operator
Chapter 3..
Methodology.
Research Design…........
Data Collection
Analysis............
Machine...
Process
Materials
Operator
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V
Chapter 4
Results..
Figure 1 Scrap Percentage Related to Machine Age.
Figure 2 Scrap Percentage Related to Machine size..
Figure 3 Scrap Levels Associated to Melt Temperature
Figure 4 Scrap Levels Related to Mold Temperature…..
Figure 5 Scrap Level Related to Pack Pressure...
Table 1 Scrap Level Related to Calibre..
Table 2 Scrap Level Related to Radel.
Table 3 Scrap Level Related to Ultem
Table 4 Scrap Level Related to Cycolac.
Table 5 Scrap Level Related to RTP .
Figure 6 Scrap Levels Related to 1st Shift Operators..
Figure 7 Scrap Levels Related to 2nd Shift Operators.
Figure 8 Scrap Levels Related to 3rd Shift Operators........
Figure 9 Scrap Levels Related with Each Production Line.
Figure 10 Scrap Levels Related to 1st Shift's A-Line Based on Experience.
Figure 11 Scrap Levels of 1st Shift's B-Line Operators Based on Experience..
Figure 12 Scrap Levels of 1st Shift's C-Line Operators Based on Experience..
Figure 13 Scrap Levels of 2nd Shift's A-Line Operators Based on Experience..
Figure 14 Scrap Levels of 2nd Shift's B-Line Operators Based on Experience..
Figure 15 Scrap Levels of 2nd Shift's C-Line Operators Based on Experience ...
Figure 16 Scrap Levels of 3rd Shift's A-Line Operators Based on Experience.
Figure 17 Scrap Levels of 3rd Shift's B-Line Operators Based on Experience.
Figure 18 Scrap Levels of 3rd Shift's C-Line Operators Based on Experience ..
Validity
Discussion.
Chapter 5 .…………………………
Conclusion
Recommendations....
References...
Appendix A.
Appendix B
Appendix C..
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Chapter 1
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Introduction
In today's business, controlling scrap is one factor that companies focus on in
order to remain competitive and maximize benefit. More specifically, in the injection
molding area, Phillips Plastics-Short Run is trying to improve scrap control. This can be
done through identifying the scrap associated with injection molding machines, plastic
processes, materials, and operators. The purpose of this research is to analyze and
identify the scrap levels related with those factors to help Short Run in better controlling
their scrap rate.
Statement of Problems
This study analyzes scrap produced at Philips Plastics-Short Run, a plastic
injection molding facility, to discover the scrap levels associated with machines,
processes, materials, and operators to help improve Short Run's scrap control.
Objectives of the Study
The objective of this research was to collect data from Phillips Plastics-Short
Run's scrap history log, analyze the scrap data, and identify the scrap levels to help
control scrap rates at Short Run.
Purpose
The purpose of this study is to help Short Run, an injection molding facility, to
identify a better solution toward the reduction of scrap. This study focuses on analyzing
the scrap related with injection molding machines, plastic processes, materials, and
operators. The results will help to identify the causes of scrap and will lead to an
appropriate solution to support Short Run in reducing scrap.
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Limitations
This study analyzes the scrap data from Short Run's scrap history log. The results
are based on 100 production samples taken at Short Run. Part mold design is not
discussed in this study. The time factor in each process will not be discussed in this study.
The post-mold operation scrap and start-up scrap are also not included in this research.
This research focuses only on the key parameters related with plastics processing.
Definitions
Amorphous Polymers A family of polymers characterized by the randomness of
entangled polymer chains.
Anisotropic Shrinkage A shrinkage that is not the same in all directions. It occurs in
fiber filled materials due to the restriction of shrinkage along the fiber length, which
tends to be in the flow direction.
Branched Polymer A polymer that has additional monomer chains protruding from its
primary chain.
Bubble Air or other gas trapped within the plastic leading to a void in the part.
Burning Showing evidence of thermal decomposition through some discoloration,
distortion, or localized destruction of the surface of the plastic.
Calibre The trade name of a polycarbonate material.
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Clamping Force The maximum holding force, expressed in tons, that a machine is
capable of maintaining.
Contamination Imperfections caused by foreign material molded into the part.
Crystalline Polymers A family of polymers characterized by areas of order in which the
molecular chains line up and lay tightly together in an otherwise amorphous mass.
Crystallization Temperature The temperature at which a crystalline resin begins to
crystallize upon cooling.
Cycle Time The time that has elapsed between the starting point in one cycle of
production and the starting point in the next cycle.
Cycolac The trade name of acrylonitrile-butadience-styrene (ABS) material.
Degradation A reduction in the physical properties of polymers due primarily to
breaking of the long chained molecules. It occurs when the resin is heated at too high a
temperature, or for too long, and can result in substandard parts.
Delamination The splitting of a plastic material along the plane of its layers. It is a
physical separation or loss of bond between laminate plies.
Engineering Thermoplastics A group of thermoplastics generally considered as high
performance materials.
Flash Extra plastic attached to a molding along the parting line.
Flow Marks A mark on a molded piece made by the meeting of two flow fronts during
molding.
Glass Transition Temperature (Tg) The temperature at which a material turns rubbery
upon heating and glassy upon cooling.
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Injection Molding A polymer processing method that produces intricate, high
performance, precise parts with very little secondary labor operations and with minimal
waste.
Melting Point (Tm) The temperature at which the crystalline regions soften and begin to
flow.
Molded-In Stress The stress that has been “built into” the part during processing.
Mold Shrinkage The amount of material shrinkage in the mold that must be
accommodated for in the tooling design and is reported in inches/inch, mils/inch, or as a
percentage.
Molecular Weight The weight of a molecule, calculated as the sum of the atomic
weights of its atoms.
Molecule The smallest unit of a substance, able to exist by itself and retain all of the
properties of the original substance. Molecules are composed of one or more atoms.
Plasticize A combination of electrical and mechanical heat energy that is used to soften
polymer pellets until they flow.
Plastics A material containing one or more organic polymeric substances of large
molecular weight.
Polymer A chemical compound formed by many small molecular units joined together to
form a large, chain-like molecule.
Polymerization A chemical reaction in which two or more small molecules combine to
form large molecules that contain repeating structural units of the original molecules.
Radel The trade name of polyerylsulfone (PES) material.
Resins Any of various materials made from polymers or plastics.
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Rheology The study of material flow.
RTP the trade name of a polycarbonate material manufactured by RTP.
Short Shot A part that is not completely filled with plastic.
Shrinkage A volume reduction of polymers that occurs during cooling due to a reduction
in space between the molecules.
Sink Marks A depression, or “dimple” due to shrinkage on a part, usually found on the
opposite side of where a thick wall section exists, caused by internal stress.
Splay Silver-streaked appearance caused by gasses in the plastic when parts are filled,
usually caused by moisture or material degradation.
Thermoplastics A family of polymers characterized by its ability to be reprocessed.
Ultem The trade name of a polyetherimide (PEI) material.
Viscosity The resistance to flow of a plastics material. It is the ratio of shearing stress to
rate of a shear.
Void Caused by internal stresses pulling plastic molecules apart.
Warpage Dimensional distortion in a plastic object after molding.
Weld Line The line in a part which results when two flow fronts meet and “knit.”
Chapter 2
Literature Review
Introduction
The analysis of most injection molding problems usually focuses on the molding
cycle (Reinhold, 1986). Typically these types of analyses are concerned with three major

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elements of the molding operation: injection molding machine, mold, and material. The
performance of these operating elements is influenced by the three variables controlling
the injection molding process: time, pressure, and temperature. They are all interrelated
variables. A change in one or more variables in the molding operation can affect the
whole process. Molding problems may also occur due to the action of operators
(Reinhold, 1986). For example, jobs that require loading inserts, pick-outs, or applying
mold release before starting the cycle, are hard to keep on a consistent cycle time.
However, through using CAD/CAM, injection molding simulation and prototyping, the
problems due to mold design are minimized (Beaumont, Nagel, Sherman, 2002). Cycle
time also depends on the response of hydraulic valves and the mechanical system of the
injection molding machine. For this reason, this research does not include process time in
the analysis. The major operating elements, machines, processes, materials, and operators
and their associated problems that cause scrap are presented in this chapter.
Machine
The basic process requirements that each injection molding machine must meet
are based on process time, temperature, and pressure (Reinhold, 1987). However,
machine characteristics may change with age (Beaumont, Nagel, & Sherman, 2002).
Scrap occurs due to inappropriate machine conditions such as a malfunctioning feed
system, inconsistent screw stop action, inconsistent screw speed, uneven back
adjustment, malfunctioning temperature control system, insufficient plasticizing capacity,
inconsistent cycle, clamp pressure not maintained, and so forth (Reinhold, 1986).
Inconsistent machine control can cause material degradation, part delamination, burning,
flash, short shot, sink marks, flow marks, etc (Reinhold, 1986).
pressure
Process
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Injection molding is a process by which plastic raw materials are converted into
useful products meeting acceptable standards (Beaumont, Nagel, & Sherman, 2002).
Each plastic material, based on type and grade, can be correctly processed within a
certain range of temperatures and pressures (Whelan, Anthon, Craft, 1978). These are the
key parameters of plastic processing. The purpose of this section is to review these key
parameters and their associated problems that can lead to scrap.
Melt temperature is the temperature at which a resin changes from a solid to a
liquid. At this point, the crystalline regions of a plastic material soften and begin to flow
(Reinhold, 1991). Melt temperatures range from 248°F to 662°F (Beaumont, Nagel, &
Sherman, 2002) and are controlled by barrel temperature, nozzle temperature, screw
speed, back pressure, and residence time.
About 70% of the heat needed to melt the plastic is generated from shear heating
that occurs within the plastic itself (Beaumont, Nagel, & Sherman, 2002). Therefore, the
melt temperature is difficult to measure and cannot be directly controlled by the
thermostats on the control panel. The injection molding machine barrel and nozzle
temperatures are maintained by electrical heating elements. These elements provide the
remaining 30% of the heat required to maintain a plastic temperature high enough to
guarantee plastic flow.
The thermodynamic properties of the molten plastic, such as viscosity, enthalpy,
and specific volume, change simultaneously with melt temperature (Johannaber, 1994).
Therefore, it is important to try and maintain a constant melt temperature in the molding
process. Any change in melt temperature leads to a change in cavity pressure, cycle time,
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or injection time. The problems associated with inconsistent melt temperatures may cause
some common part defects such as splay, burning, flash, flow line, short shot, sink marks,
bubbles, etc (Reinhold, 1996).
Mold temperature is the temperature that maintains the cavity surface at a
specified temperature to cool a hot plastic to a solid state. Mold temperatures range from
32°F to 302°F, and are dependent on the coolant temperature, flow rate, proximity of the
coolant channels to the plastic, and the rate of the heat input from the plastic. The coolant
flow rate reaches its maximum if the fluid is in the state of turbulent flow. The flow can
be characterized by calculating the Reynold's number for the stream. It is the ratio of
inertia forces to viscous forces within the flow field. The Reynold's number is a
dimensionless number based on the channel diameter, flow rate, density, and viscosity of
the fluid. If this number is greater than 10,000 (Reinhold, 1996), turbulent flow is fully
developed and the co-efficient of the heat transfer is maximized (Beaumont, Nagel, &
Sherman, 2002). Heat transfer may be satisfactory when the mold is new, but it will
decrease as the mold ages due to corrosion and lime deposits. The heat input from the
plastic varies from location to location. It depends on the local part thickness and the
plastic flow past the location. The mold wall temperature is not uniform, and hence the
cooling rate will not be uniform. This can affect the melt viscosity, cavity pressure, or
hold pressure (Johannaber, 1994). These problems can cause part defects such as sink
marks, void, bubble, warpage, short shot, flow line, surface defects, etc (Reinhold, 1986).
In many plastic injection molding machines, a hydraulic pressure is applied to
force the screw forward against the melted plastic. The plastic is forced to flow through
the nozzle, the sprue, the runner system, and finally into the cavity to form the part
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(Beaumont, Nagel, & Sherman, 2002). This pressure ranges from 7,250 pounds per
square inch (PSI) to 36, 260 PSI. Due to the way a plastic fills and solidifies within the
mold cavity, pressure is not uniform throughout the part. The highest pressure occurs at
the gate; the lowest at the point in the cavity to fill last. The total volume of plastic in the
cavity tends to be reduced as it cools and solidifies. Pack and hold pressures are used to
provide a compensation flow into the cavity to make up for lost volume as the plastic
shrinks with decreasing temperature and while the gate remains open. However, to
minimize volumetric shrinkage in the cavity, pressures are minimized to the point where
there is enough pressure remaining to provide a compensating flow but not to where it
tends to over-pack the material near the gate. Insufficient pressures can cause part
brittleness, bubbles, sink marks, cracking, flashing, short shot, etc. (Reinhold, 1986).
Material
Plastic materials consist of two basic groups, thermoplastics and thermosets.
Thermoplastic materials are made of the linear or branched polymer units comprised of
repeating monomers. They comprise about 94% of the volume of the material used in the
plastic industry and can be repeatedly heated, melted, and formed into a product.
(Beaumont, Nagel, & Sherman, 2002).
Thermoplastics include amorphous polymers and semi-crystalline polymers.
Amorphous resins have a wide processing temperature window. An amorphous polymer
chain is randomly entangled. Typical amorphous polymers are polystyrene, acrylonitrile-
butadience-styrene (ABS), polyethersulfone, etc. Crystalline resins, on the other hand,
have a narrow processing temperature window. Their molecular chains lie side by side in
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a highly oriented fashion. Well-known examples of crystalline polymers are
polypropylene, acetal, and polytetrafluoroethylene (Brydson, 1999)
Thermoset materials react chemically during processing to form a cross linked
structure. They cannot be melted and reprocessed (Reinhold, 1991). Polyimides,
polyesters, and epoxies are examples of thermoset materials.
The transition between solid and liquid phases is a primary concern when
processing plastics. In crystalline materials, the change from solid to liquid is abrupt and
easily discernible. In an amorphous polymer, the material softens over a wide
temperature range. In polymer science, there is a point called the glass transition point
(Tg). At temperatures below this point, plastic is stiff, stable, and behaves like a solid. In
environments at temperatures above the Tg, the polymer will behave as a viscous liquid
(Reinhold, 1991).
Within a material, there are two forms of energy (Reinhold, 1991) used to
maintain the physical structure. One is potential energy, which is a measure of the forces
of attraction between the molecules. The other is kinetic energy, the energy of motion
tending to separate the molecules. As more energy is put into the system, it turns into a
liquid. That is where the potential and kinetic energies are equal.
Thermoplastic materials are made of strong covalent bonds (primary bonds) along
polymer molecules and weaker secondary bonds (Van der Waals' forces) between
polymer molecules (Beaumont, Nagel, & Sherman, 2002). A covalent bond exists when
two atoms share the electrons in their outer shells in order to be stable. It has a
disassociation energy of 83 Kcal/mole. The Van der Waals' forces are electrostatic in
nature and have a disassociation energy of 2-5 Kcal/mole. This is the energy that attracts
16
molecules (cohesive energy), and is also the energy required to move a molecule a large
distance from its neighbor (Reinhold, 1991).
If the temperature of a plastic rises, the distance between the molecules increases.
Because the Van der Waals' forces decrease with the sixth power of the distance, the
molecules and their segments become more mobile. As these forces decrease in an
exponential manner, there is a relatively narrow range in which the polymer changes
from solid to a liquid. Therefore, polymer properties are quite temperature-dependent
(Reinhold, 1991). For this reason, it is important to know the processing temperature
range for each plastic material in order to make good parts.
During the injection molding process, a polymer mass is heated to a point at
which it melts. In this molten phase, the material can flow and is forced into a cold mold
where it will take the shape of the cavity (Beaumont, Nagel, & Sherman, 2002).
However, a resistance to the flow of plastic material, exists due to viscosity (Brydson,
1999), which is determined by shear stress divided by shear rate. Shear stress is a
measure of the resistance to flow of the molecules sliding over each other (Reinhold,
1991). Shear rate is the rate of velocity change of a flowing material.
For a specific polymer, the viscosity is dependent on temperature, molecular
weight, and shear rate (Brydson, 1999). The higher the temperature, the lower the
viscosity. The higher the molecular weight, the greater the entanglements and the greater
the melt viscosity. To maintain the same volume of material in the cavity, shot after shot,
it is necessary to maintain the consistency of pressure and viscosity. However, the
characteristics of materials are very complex (Beaumont, Nagel, & Sherman, 2002) and
most of them are non-constant. Non-constant viscosity is affected by the molecular
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weight distribution of a polymer. This is a factor that makes it difficult for a process
engineer to create an optimum process.
State-of-the-art tools such as material databases and injection molding simulation
software are available to aid in the prevention of common problems. However, the non-
constant and complexity in characteristics of plastic material, combined with the process
conditions in manufacturing, still result in unacceptable parts. Common part defects
include contamination, burning, bubbles, splay, sink marks, voids, short shot, and
warpage (Reinhold, 1986).
Operator
Reinhold wrote, “If the problem appears, disappears, or changes with the
operators, look for the differences in actions of operators." (1986, p 665) Operator actions
are the methods by which operators perform their jobs, and these actions can be related to
machine performance. This research reviews the operator experience-performance
relationship and uses it as a tool for analyzing the relationship between operator and scrap
levels. The only factor relating to operators that this research focuses on is work
experience based on the time spent on the job.
Most literature on work experience has focused on time (79.5%) or job level of
specificity (68.2%), (Kolz, McFarland, & Silverman, 1998). Job experience was defined
as a number of years an employee had worked in the same job for the same company.
This is the most commonly used definition of job experience. However, the jobs
consisted of a limited number of activities and rarely deviated from their routine; the
number of years on the job was highly related to the number of times each work task was
performed. This agreed with the results showing that the number of times a person
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performs a job task is more strongly correlated with work performance than the time
spent on the job. Data on the number of years on the job is readily available. Therefore, it
is a more practical measure of experience rather than counting the number of times a task
is performed. For this reason, the years on the job are likely to continue to be an
important measure of experience.
Work experience can be measured based on time, amount, or type (Kolz,
McFarland, 1998). In a time-based mode, experience is measured by the time spent in a
particular job, company, or given occupation. In an amount-based measure, the
experience of an operator can be measured as the number of times he/she performs a
particular task. Some studies measure an individual's work experience based on type.
This measurement mode defined experience as the degree of similarity between a
person's previous job and current job. The more similar the previous job is to the current
one, the more relevant work experience the person is presumed to bring to the current
job.
Work experience has also been measured at the task, job, or organizational level
of specificity (Kolz, McFarland, 1998). At a task level of specificity, work experience is
measured as the number of times an individual performed a task. At a job level,
experience is measured by the amount of time an individual spent on a job. At the
organizational level of specificity, experience is measured as the time a person spent in
an organization.
The results showed the strongest relationship between experience and
performance was when work experience was measured at an amount or task level of
specificity. The meta-analysis also reveals that the relationship between work experience
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and job performance was positive regardless of the work experience measure used
(Quiñones, Ford, & Teachout, 1995). In other research, conducted by Hofman, Jacob, &
Baratta, It was concluded that individuals may rate an employee's performance relating
to his/her level of experience (1993). In addition, a meta-analysis by McDaniel, Schmidt,
& Hunter (1998) found a mean corrected correlation of 32% between work experience
and job performance across a number of occupations.
In the injection molding process, there are cases where the operators need to
manually operate the injection molding machines. For example, an operator has to open
the machine door to take the part out of the mold. They need to put in inserts, pick-outs,
or apply mold release before starting the next cycle. Such actions by operators may result
in changing the cycle time, residence time, temperature, and viscosity of the plastic
material. These problems will result in several part defects such as splay, burning, short
shot, sink marks, surface defects, and so forth (Reinhold, 1986).
Chapter 3
Methodology
This chapter will present the methods and procedures used to identify the scrap
levels associated with each major factor: machine, process, material, and operator. The
information is based on scrap data collected from the scrap history log at the Phillips
Plastics-Short Run facility. Data was organized and used to calculate average scrap levels
related to each factor for this analysis. Results will be discussed to address the causes of
the problems that lead to scrap.
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Research Design
The data from hundreds of production jobs was collected randomly from
September through November 2003. However, to assure that a good statistical sampling
of data was gathered, at least three jobs for each machine were collected. To guarantee
consistency when gathering data, each production job was run through all shifts. The data
collected includes material type and key process parameters: melt temperature, mold
temperature, and pressure. Information about machine age and size or tonnage for all 32
injection molding machines was collected. Operator data for the facility's first, second,
and third shifts was obtained according to their years of experience.
Data Collection
With permission from the plant and production managers, maintenance
coordinator, and supervisors of all three shifts at Phillips Plastics-Short Run facility, data
was collected from Short Run's scrap history logs for September to November, 2003. The
data included: operator initial and shift run, total good part, total scrap, and scrap caused
by common problems like contamination, partial fill, void/bubbles, sink marks, burning,
and splay. The material type, process key parameter, melt temperature, mold temperature,
and pressure were also included with the data (Appendix A). In addition, age and tonnage
from all injection molding machines on the floor were collected (Appendix B). The list of
operators and their years of experience was also collected (Appendix C).
For this study the data was collected randomly from one hundred production jobs.
However, to assure that a good statistical sampling of data was taken, at least three
production samples were collected from each machine in an effort to include every

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machine in this research. Although limited data can be gathered from a real world
business, the information collected satisfied basic statistical and research requirements.
Analysis
The data collected was organized and grouped in a manner that addressed each of
the major factors covered in this research: machine, process, material, and operator. Then
the scrap was organized and analyzed based on the appropriate requirements of each
factor to yield their scrap levels.
Machine
To analyze the scrap related with the injection molding machines, the percentage
scrap related with each machine was calculated. Then the machines were organized into
four groups based on their tonnage and age at their associated scrap level. Group one
consisted of machines two years old or less. Group two included machines from three to
four years of age. Group three included machines from five to eight years of age. Finally,
group four included the oldest machines, which consisted of eleven to fourteen years
operation. The average scrap percentage related with these groups was calculated for an
overview of the scrap level trends associated with the age of machines.
To analyze the scrap level related with the machine tonnage, machines were
organized into following five groups:
• Group one: 20-40-ton machines.
of
·
Group two: 55-80-ton machines.
. Group three: 110-150-ton machines.
.
Group four: 200-300-ton machines.
•
Group five: only one machine of 400 tons.
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The average scrap level, in percentage, was calculated and yielded the scrap trend
associated with the machine tonnage from low to high.
Process
This area of research focused only on the analysis of key process parameters in
the injection molding process conditions. These parameters include melt temperature,
mold temperature, and pressure.
Melt Temperature
The melt temperature of the process in this research is classified into three levels:
under 500°F, 500-600°F, and over 600°F. The scrap levels associated with each range of
temperature were calculated to identify trends.
Mold Temperature
The mold temperatures are presented at three levels: under 100°F, 100-200°F, and
over 200°F. The scrap levels related with the mold temperatures were calculated for each
range to identify trends.
Pressure
The pressures were organized into three ranges: pressures under 10,000 PSI,
10,000-20,000 PSI, and over 20,000 PSI. Good and scrap part rates associated with each
range of pressure were calculated to get the average scrap percentage. The results identify
a trend of scrap levels associated with the process pressure.
Materials
The majority of materials used in the one hundred production samples collected
for this research consisted of the following materials: Calibre, Radel, Ultem, Cycolac,
and RTP. Other materials used with less frequency in the production run were Lexan,
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Bayblend, LNP, Lustran, Cycoloy, Zytel, Santoprene, etc. Only the first five materials are
analyzed for this study. The data related with each of these five materials was organized
to yield their specific scrap levels. The scrap rate related to common defects, such as
contamination, partial fill, void/bubbles, burn/streaks, sink marks, and splay, was also
calculated to identify relationships between these material defects.
Operator
To analyze the scrap associated by operator; this research organized operators on
each production line based on their years of experience. Operators were divided into three
groups: less than one year of experience, one to two years of experience, and over two
years of experience. The scrap percentages for each operator were calculated, and then
identified for each group. The results show a relationship exists between scrap levels and
operator experience. The average scrap levels associated with operators on each
production line and shift were also calculated and analyzed.
Chapter 4
Results
This chapter presents a detailed overview of the scrap levels associated with
machine, process, material, and operator. The scrap levels are related to the tonnage or
age of injection molding machines. The scrap percentages are also related to plastic
process key parameters: melt temperature, mold temperature, and pressure. The scrap
levels associated with the five most common materials, used by Phillips Plastics-Short
Run facility, were used for this research. And the scrap associated with operators, on each
shift and production line, was based on their years of experience. These results, based on
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24
the analysis of actual scrap data, can be used by Phillips Plastics-Short Run to quickly
predict the levels of scrap that may occur at each work station. Therefore, they will be
able to better control the generation of scrap at their work stations.
The scrap rates associated with machine age are shown in Figure 1. The scrap
rates related with using the newest machine (1-2 yrs) were quite high. The scrap rates
were lowest using the 2-4 year old machines. Scrap level related with using the machines
over 5 years of operating age were similar, at above 5%. Except for the machines under 2
years of age, scrap level tends to increase as machines get older.
Scrap (%)
18
16
14
8 6420
12
10
8
16.5
Scrap % Related to Machine Age
CO
6
5.1
5.4
3.6
4
2
0
1-2
2-4
5-8
11-14
Age (yr)
Figure 1 Scrap Percentage Related to Machine Age
The results show in figure 2 that the scrap level increases as the tonnage of the
machine increases. The machines less than 40 tons in size resulted in the lowest level of
25
scrap. Machines from 55-80 tons in size resulted in 5.9% of scrap. Machines 110-150
tons in size resulted in a scrap level of 5.8%. Machines 200-300 tons in size resulted in a
7% scrap level. Only one 400-ton machine operates on the shop floor. The scrap related
with it was high, up to 34%. However, just one machine at that clamp force does not
result in a good statistical sampling. In general the trend of scrap increases as the
machines' tonnage gets higher.
Scrap (%)
Scrap Level Related to Machine size
40%
30%
20%
10%
5.90% 5.80%
7.00%
4.20%
☐
0%
34.0%
20-40 55-80 110-150 200-300 40
Size (ton)
Figure 2 Scrap Percentage Related to Machine size
Figure 3 shows the scrap levels associated with the melt temperature. In the range
of melt temperatures under 500°F, the scrap level was 0.8%. The scrap jumped to a
higher level of 3.9% with the melt temperatures between 500-600°F. And with the melt
temperature over 600°F, the scrap again increased to a level of 5.3%. In the common
range for melt temperature (under 500°F), the scrap was at an acceptable level. At higher
26
46
temperatures, the scrap levels increased. The apparent trend is that the higher the melt
temperature, the higher the scrap level.
Scrap (%)
Scrap Level Related to Melt Temperature
6%
5.3%
5%
3.9%
4%
3%
2%
0.8%
1%
0%
under 500
500-600
over 600
Temperature (°F)
Figure 3 Scrap Levels Associated to Melt Temperature
Figure 4 presents the average scrap percentage results associated with mold
temperatures. At lower mold temperatures (under 100°F), the scrap level reaches a very
high level of 8.6%. The scrap percentage reduces to about half (at 4.7%) in the mid-range
of mold temperatures (100 °F -200°F). At higher mold temperatures (200°F and up) the
scrap level was 2.9%. Therefore, it is apparent that the higher the mold temperature, the
lower the scrap level.
Scrap (%)
Scrap Level Related to Mold Temperature
10%
8.6%
8%
6%
4.7%
4%
2.9%
2%
0%
under 100 100-200 over 200
Temperature (°F)
Figure 4 Scrap Levels Related to Mold Temperature
As Figure 5 shows, at the lower range of pressures (under 10,000 PSI), the scrap
level was very high at 9.3%. At the mid-range of pressures (10,000-20,000 PSI), the
scrap was lower at 3.7%. The process at higher pressures, 20,000 PSI or higher, resulted
in a scrap level of 4.8%. In general, the scrap level was lowest at pressures of 10,000PSI
to 20,000PSI. The processes that require higher pressures produce higher level of scrap.
However, at a lower pressure (under 10,000 PSI) the scrap level also becomes very high.
The five most commonly used materials for this research were Calibre, Radel,
Ultem, Cycolac, and RTP. Calibre was the most commonly used material in the data
collected for this research. Table 1 show that the over all scrap level associated with
using this material was 3%. The contamination level related with this material resulted in
the highest specific scrap level. The scrap level due to burning, void/bubble, and splay
were also monitored. Scrap levels due to partial fill were very low using this material,
27
28
and scrap due to sink marks was nonexistent. Generally, Short Run should pay very close
attention to contamination of material, then consider scrap due to burning, void/bubble,
and splay when using this material.
Scrap(%)
Scrap Level Related to Pack Pressure
10%
9.3%
8%
6%
4.8%
3.7%
4%
2%
0%
under 10,000 10,000-20,000 over 20,000
Pressure (PSI)
Figure 5 Scrap Level Related to Pack Pressure
Total Parts Contamination Partial Void/Bubble Burn/Streak Sink Splay Scrap Rates
203,707
1844
52
256
318
0 203
3.0%
Table 1 Scrap Level Related to Calibre
Radel was the second most commonly used material at the Short Run facility, as
identified by this study. The over all scrap level related with the use of this material was
29
4.6%. Splay resulted in the most scrap. Scrap due to contamination was the second most
important issue when using this material.
Total Parts Contamination Partial Void/Bubble Burn/Streak Sink Splay Scrap Rates
8,387
59
14
7
1
0
138
4.6%
Table 2 Scrap Level Related to Radel
Ultem was another material used often by Short Run. The study shows that the
over all scrap level related with using this material was 5.3%. Most scrap problems
occurred due to splay. The next problem occurred due to contamination scrap level.
Void/Bubble and burn/streak scrap levels were much lower than splay and contamination
scrap levels. For this material, scrap levels due to sink marks and partial fill were very
low. Therefore, splay and contamination should be closely monitored when using Ultem.
Total Parts Contamination Partial Void/Bubble Burn/Streak Sink Splay Scrap Rates
102,519
245
26
97
63
18 840
5.3%
Table 3 Scrap Level Related to Ultem
Table 4 shows that the over all scrap level associated with using Cycolac was
2.5%. The most common scrap problem presented with using this material proved to be
splay. Contamination was far less a problem, but nevertheless also needs to be
considered. Similar to Ultem, when Cycolac was used, the splay scrap levels were
highest.
30
Total Parts Contamination Partial Void/Bubble Burn/Streak Sink Splay Scrap Rates
39,056 72 15 3 2 3 420 2.5%
Table 4 Scrap Level Related to Cycolac
The over all scrap level related with using RTP is presented in Table 5, and was
found to be 9.3%. The table also shows the biggest problem was scrap due to
contamination. Sink marks and partial fill scrap levels should also be considered. Splay,
bubble, and burning scrap levels were rarely problematic when using this material.
Therefore, most scrap reduction efforts should be focused on contamination during the
use of RTP.
Total Parts Contamination Partial Void/Bubble Burn/Streak Sink Splay Scrap Rates
13,184
454
178
0
13
193
5
9.3%
Table 5 Scrap Level Related to RTP
Figure 6 shows the scrap percentage related with three lines of 1st shift production
at Short Run. The scrap level on A-line was found to be 2.9%. On B-line, the scrap
percentage jumped to a higher level of 4.6%. And on C-line, the scrap level resulted in a
rate of 3.5%. These scrap rates resulted in an average scrap rate of 3.7% for the first shift.

Scrap(%)
5%
Scrap Level Related to 1st Shift Operator
4.6%
4%
3.5%
2.9%
3%
2%
1%
0%
A-Line
B-Line
C-Line
Production Line
Figure 6 Scrap Levels Related to 1st Shift Operators
The result in figure 7 show that the scrap percentages for 2nd shift as related to
operators were: 6.8% (A-line), 9.6% (B-line), and 7.5% (C-line). B-line, again garnered
the highest percentage of scrap level. The next lower scrap level was C-line, and at yet a
lower scrap level was the A-line. On average, the scrap level on 2nd shift was 8%.
The results for 3rd shift, shown in figure 8, at Short Run were: 4.7%, 8%, and
4.2% associated with A, B, and C-lines, respectively. The highest level of scrap still
occurred with the B-line. However, A and C-lines were extremely close to each other, at
4.7% and 4.2%, respectively. The results also show an average scrap percentage of 5.6%
for 3rd shift.
31
Scrap(%)
Scrap(%)
12%
Scrap Level Related to 2nd Shift Operator
9.6%
10%
7.5%
8% 6.8%
6%
4%
2%
0%
A-Line
B-Line
C-Line
Production Line
Figure 7 Scrap Levels Related to 2nd Shift Operators
10%
8%
6%
4%
2%
Scrap Level Related to 3rd Shift Operator
4.7%
8.0%
لت
4.2%
ili
0%
A-Line
B-Line
C-Line
Production Line
Figure 8 Scrap Levels Related to 3rd Shift Operators
The average scrap level for each production line on all three shift is shown in
figure 9. It can be seen that the average percentage scrap level for the A-lines on all shifts
was 3.7%. The B-lines reached an 8% average and the C-lines yielded a 5.6% scrap level
32
32
33
associated with all three shifts. Generally, Figure 9 shows the highest scrap level occurs
for B-line, lowest on A-line, and C-line falls in between.
Scrap(%)
Scrap Level Related to each Production Line
10%
8%
8.0%
5.6%
6%
3.7%
4%
2%
0%
A-Lines B-Lines
C-Lines
Production Line
Figure 9 Scrap Levels Related with Each Production Line
Data gathered on operator experience for A-Line 1st shift is shown in figure 10.
This data was organized into three groups based on their years of experience:
• Group 1: includes the operators that had less than a year experience.
Group 2: includes the operators that had 1 to 2 years of experience.
• Group 3: includes the operators that had over 2 years of experience.
Figure 10 shows only two groups because there were no operators with less than one year
of experience. The group of operators having from 1 to 2 years experience resulted in a
scrap level of 3.2%. The other group having over 2 years of experience was associated
with a scrap level of 2.1%. Figure 10 provides evidence that operators with more than 2
years of experience generated less scrap.
Scrap (%)
Scrap Level Related to Operator Experience
5.00%
4.00%
3.2%
3.00%
2.10%
2.00%
1.00%
0.00%
1-2 Years Over 2 Years
Experience (Yr)
Figure 10 Scrap Levels Related to 1st Shift's A-Line Based on Experience
34
==
Figure 11 shows the scrap levels related to three operator groups for 1st shift B-
line. This study was organized into the following groups:
• Group 1: operators that had less than 1 year of experience resulted in 3% scrap.
•
Group 2: operators that had from 1- 2 years of experience resulted in 3.4% scrap.
• Group 3: operators that had over 2 years of experience resulted in 4.4% scrap.
Surprisingly, Figure 11 shows that the more experienced operator generated the higher
scrap level. The fact that a more experienced operator generated the highest scrap level
was an unexpected trend.
Scrap(%)
Scrap Level Related to Operator Experience
5%
4.4%
4%
3.4%
3.0%
3%
2%
1%
0%
Under 1 year 1-2 years
Over 2 years
Experience (Yr)
Figure 11 Scrap Levels of 1st Shift's B-Line Operators Based on Experience
Figure 12 shows the relationship between operator experience and scrap levels for
1st shift C-line. This data was organized into the following groups:
•
•
Group 1: operators that had under 1 year of experience resulted in 5.2% scrap.
Group 2: operators that had 1-2 years of experience resulted in 3.7% scrap.
• Group 3: operators that had over 2 years of experience resulted in 2.0% scrap.
The results presented in Figure 12 show that the higher the operator's experience, the
lower the scrap level. Based on the operator capabilities due to experience, this is an
expected trend in the generation of scrap.
35
Scrap(%)
Scrap Level Related to Operator Experience
6%
5.2%
5%
3.7%
4%
3%
2%
1%
0%
2.0%
Under 1 year 1-2 years Over 2 years
Experience (Yr)
Figure 12 Scrap Levels of 1st Shift's C-Line Operators Based on Experience
Figure 13 presents the scrap levels related to 2nd shift A-line, based on operator
experience. The data was organized in the following groups:
•
Group 1: operators that had under 1 year of experience resulted in 9.4% scrap.
Group 2: operators that had 1-2 years of experience resulted in 7.2% scrap.
• Group 3: operators that had over 2 years of experience resulted 1.3% scrap
The trend shows a good relationship between operator's experience and their scrap
levels. As expected, the more experienced operators produced less scrap.
36
36
Scrap(%)
12%
Scrap Level Related to Operator Experience
10% 9.4%
8%
6%
4%
2%
0%
7.2%
1.3%
Under 1 year 1-2 years Over 2 years
Experience (Yr)
Figure 13 Scrap Levels of 2nd Shift's A-Line Operators Based on Experience
Figure 14 presents two groups of operators for 2nd shift B-line and their related
scrap percentage, based on their experience. In this particular case, there was no group of
operators with 1 to 2 years of experience. The results show a scrap level of 6.3% for the
group of operators having less than 1 year of experience. The group of operators having
over two years of experience generated scrap at a 11.3% level. Once again, the trend here
is that the higher experienced operators produced more scrap. This trend is counter
intuitive to what was expected, scrap levels should decrease as operator experience
increases.
Figure 15 presents the scrap levels associated with two groups of operator for 2nd
shift C-line. One group had from 1 to 2 years experience. The scrap level for this group
resulted in an 11.2% scrap level. The other group consisted of operators with over 2 years
of experience. The scrap level for this group resulted in a 6.6%. Figure 15 also shows an
37
Scrap(%)
expected trend. The 2nd shift C-line operators with the most experience generated the
least scrap.
Scrap(%)
Scrap Level Related to Operator Experience
14%
11.3%
12%
10%
8%
6.3%
6%
4%
2%
0%
Under 1 year
Over 2 years
Experience (Yr)
Figure 14 Scrap Levels of 2nd Shift's B-Line Operators Based on Experience
14%
Scrap Level Related to Operator Experience
12%
10%
8%
6%
4%
2%
0%
11.2%
6.6%
li
1-2 years Over 2 years
Experience (Yr)
Figure 15 Scrap Levels of 2nd Shift's C-Line Operators Based on Experience
38
39
Figure 16 shows the scrap levels related with the operators on 3rd shift A-line. The
data was organized by operator experience into the three following groups:
•
•
Group 1: operators that had under 1 year of experience resulted in 2.2% scrap.
Group 2: operators that had 1-2 years of experience resulted in 5.7% scrap.
Group 3: operators that had over 2 years of experience resulted 5.2% scrap
These results are inconsistent in regards to the expected relation between operator
experience and scrap levels. The group of operators having the least experience resulted
in the lowest level of scrap. The group having 1-2 years of experience resulted in the
highest level. The group of operators having over 2 years of experience resulted in a
slightly lower scrap level. In general, the trend witnessed here is that the more
experienced operators made more scrap.
Scrap(%)
Scrap Level Related to Operator Experience
8%
7%
5.7%
6%
5.2%
5%
4%
3%
2.2%
2%
1%
11
0%
Under 1 year
1-2 years
Over 2 years
Experience (Yr)
Figure 16 Scrap Levels of 3rd Shift's A-Line Operators Based on Experience
40
Figure 17 illustrates the relationship between operators and their related scrap
levels for 3rd shift B-line. An irregular trend can be witnessed here. The least and most
experienced groups generated similar levels of scrap, 11.0% and 10.4% respectively. The
group of operators that had 1-2 years of experience resulted in the scrap percentage of
4.3%. Again, these results do not show a consistent relationship between operator's
experience and scrap.
Scrap(%)
Scrap Level Related to Operator Experience
14%
12% -11.0%
10.4%
10%
8%
6%
4.3%
4%
2%
0%
Under 1 year 1-2 years Over 2 years
Experience (Yr)
Figure 17 Scrap Levels of 3rd Shift's B-Line Operators Based on Experience
Figure 18 presents the scrap levels related with three groups of operators on 3rd
shift C-line. Based on their experience, this data is summarized below:
•
•
•
4.6% scrap level for the group with under a year of experience
3.0% scrap level for the group with 1-2 years of experience
10.8% scrap level for the group that has over 2 years of experience

41
The first two groups depict an expected trend about the relationship between operator's
experience and scrap percentage. However, as seen previously, the highest scrap level of
10.8% was generated by the most experienced operators. This result again is counter
intuitive to what is expected in the generation of scrap and based on operator experience.
Scrap(%)
Scrap Level Related to Operator Experience
12%
10%
8%
6%
4.6%
4%
3.0%
2%
0%
10.8%
Under 1 year 1-2 years Over 2 years
Experience (Yr)
Figure 18 Scrap Levels of 3rd Shift's C-Line Operators Based on Experience
Validity
The research presented here is based on real data gathered from a Phillips
Plastics-Short Run facility. The data was organized and analyzed based on the statistical
process control that has been applied in the real-world manufacturing operations at the
Short Run facility. Due to the fact that this Short Run facility continually monitors their
scrap levels, it is possible to have a high level of confidence in the data gathered.
This research can be used by Short Run production to better understand why scrap
levels vary for production jobs run with the specific process parameters identified in this
42
work. Short Run production personnel, such as machine operators, mold technicians, and
supervisors, will be able to use this work to minimize the generation of scrap. Every
production job will be prepared in a way that will reduce the problems by
acknowledgement of the related scrap levels with the type of injection machine, process,
material, and operator involved in each production job at specific work stations.
Discussion
This section of the research discusses the reasons for the varying scrap levels seen
in production related to the machine, process, material, and operator. By understanding
the root causes of the problem, Short Run can determine more predictable ways in using
these production resources, ultimately resulting in a better control of scrap generation.
Machines
The findings of this research indicated that the scrap levels vary based on machine
age and tonnage. The data gathered supports the concept that the longer a machine is in
operation, the less efficient it becomes. The machine response time becomes inconsistent
with age. Therefore, the machine itself changes the processing conditions, resulting in an
increase of scrap. At Short Run, an injection molding facility, scrap increased from a rate
of 3.6% to 5.4% with machines that had been in operation from 2 to 14 years. An
unexpected result identified when evaluating the production data was that newer
machines (1-2 years old) resulted in a very high scrap level of 16.5%. These newer
injection molding machines included a vertical machine and a 400-ton machine. Most of
the time, these machines must run in a semi-automatic function mode. The reason for the
higher scrap levels associated with using these machines was due to the way operators
operate the machines. Differing operator actions made it difficult to keep the cycle times
43
consistent. This inconsistency in cycle time was the reason for processing condition
changes, resulting in an increase of scrap generation.
Another factor identified in this research that lead to scrap generation involved
machine size or tonnage. This factor is an indicator of the machine's strength. Jobs
requiring a stronger machine are usually complicated in shape, mold design, and part
design. The polymer flow pattern of larger parts is usually quite complex, requiring
higher processing pressures to fill mold cavities and greater machine strength. Due to the
complexity of these larger parts, they must be made in a semi-automatic function mode
because of the necessity of loading the pick-outs, inserts, etc. For these reasons it was
difficult for the operators running these jobs to keep cycle times consistent. When one or
a combination of these machine factors existed in production, the scrap level may have
risen. Based on the recently discussed items it is possible to make a rationalization as to
the reason that the use of larger machines can often lead to increased levels of scrap
generation.
Process
This portion of the research focuses on analyzing the key process parameters of
melt temperature, mold temperature, and pressure. Though process time can lead to other
issues of concern, it is easy to control. Problems can occur based on how machines
respond to each change in setting. If the machine does not respond well, possibly due to
its age, the time setting may not work resulting in molding problems.
Melt Temperature
The research findings shows that the higher the melt temperature, the higher the
scrap level. Most of the melt temperature induced problems can be related to melt
44
temperatures higher than 500°F, especially when the temperature was higher than 600 °F.
This occurs because most thermoplastics require that the processing temperatures be less
than 500°F. Melt temperatures higher than 500°F are considered to be excessively high
temperatures. With the higher temperatures, the covalent bonds of the resin molecules are
more likely to degrade in molded materials. Therefore, the chances of splay, burning, or
shrinkage problems occurring may be higher than when processing at lower temperatures.
It is for this reason that higher melt temperatures typically lead to higher scrap levels.
Mold Temperature
The research findings show that when higher mold temperatures were used the
resulting scrap level was lower. Scrap levels were lowered because the use of higher
mold temperatures lead to a reduction in material shear rate. Therefore, the in-mold
material flows occur more smoothly. Problems such as short-shot, surface finish, over-
sizing, etc, may be reduced by increasing mold temperatures.
Pressure
Machine pressures between 10,000 PSI to 20,000 PSI are applied for processing
of most thermoplastics. Most parts require pressures in this range to guarantee adequate
in-mold material flow. Pressures should be great enough to keep the cavity filled but not
so much that over-packing occurs. If a particular process requires a higher pressure (over
20,000 PSI) to meet the requirements of a complex flow pattern, it usually causes higher
material shear rates or more material crystallization around the gate. These problems can
cause part splay, crack, or warpage. For this reason higher machine pressures typically
lead to higher scrap rates. The results also show a trend towards high scrap levels (9.3%)
related to using machine pressures that are less than 10,000 PSI. Too low a machine
45
pressure usually leads to slower material fill rates and improperly filled or packed parts.
Not enough plastic is added during the mold fill process to compensate for part shrinkage
when too low a pressure is used. This can be the reason of material short shot, shrinkage,
or sink marks.
Materials
In a real-world plastics manufacturing facility, like Short Run, quite a few
material types are used to produce plastic parts. In an attempt to keep the analyses
performed for this research manageable, this study covers the five most commonly used
materials at Short Run. These materials consist of Calibre, Radel, Ultem, Cycolac, and
RTP. The scrap levels associated with each of these five materials, listed from worst to
least, were as followed:
.
RTP at 9.3% scrap
•
Ultem at 5.3% scrap
•
Radel at 4.6% scrap
•
Calibre at 3.0% scrap
• Cycolac at 2.5% scrap
Cycolac
It is
easy to understand why the use of Cycolac as a material resulted in a low
scrap level of 2.5%. By examining the data collected, it can be seen that the processing of
Cycolac required a temperature range from 400 °F to 500°F. As discussed earlier in the
literature review section, this is a common processing temperature range that is
applicable for most plastic materials.
46
The mold temperature required for processing this material ranged from 50 °F to
150°F. Most of the productions runs, based on the data collected for this research, were
completed using a mold temperature of about 100 °F. This was another advantage of using
this type of material. The pressures applied for processing this material ranged from
5,500 PSI to 21,000 PSI. For most of the productions runs pressure ranged from about
10,000 PSI to 15,000 PSI. This range of processing pressures is common for pack and
hold pressures used to process most plastic materials. In general, the key parameters used
to control the processing of Cycolac, melt temperature, mold temperature, and pressure,
were within common process conditions. Therefore, the 2.5% of scrap associated with
processing Cycolac can be explained by looking at its key processing parameters.
Because Cycolac is hygroscopic it is susceptible to the occurrence of splay,
contamination, or short shot when used to produce parts, and ultimately is the primary
reason for producing degraded and undesired parts.
Calibre
Calibre is the most commonly used production material at Short Run. A scrap
level of 3.0% was seen with the use of Calibre. The most common problems to occur
when using this material consisted of contamination, burning, splay, and voids/bubbles.
These issues can be explained by taking a look at material processing parameters. The
melt temperature used to process this material ranged from 530°F to 600°F. Mold
temperatures ranged from 70°F to 190°F. Pressures ranged from 11,000 PSI to 25,000
PSI. In comparing these processing parameters to those used for Cycolac, it can be seen
that the values for all three parameters had increased slightly. These results imply that the
use of a higher mold temperature resulted in a lower scrap level. Therefore, it can be seen
47
that the mold temperature-scrap relation is not an issue when processing Calibre.
However, the melt temperatures and pressures required for processing Calibre can be
related to the generation of scrap. The higher that the melt temperature or pressures are
the higher the resulting scrap levels. Again, by closely examining the process parameters
used to produce Calibre parts, it is possible to explain the low scrap level of 3%.
Radel
The use of Radel in producing parts resulted in a scrap level of 4.6%. The most
common reason for scrap generation was the occurrence of splay. The next most common
reason for problems occurred due to contamination and short shot. It is easy to
understand why the scrap levels related to using this material were higher than the scrap
levels that occurred when using Cycolac or Calibre. By examining the process melt
temperature, ranging in value from 670°F to 740°F, required for producing Radel parts, it
is possible to gain insight into the reasons for an increase in scrap generation. It can be
seen that fairly high temperatures were used to produce Radel parts, causing the material
in the barrel to easily degrade or burn. For this reason, an increase in the occurrence of
splay or contamination was seen with the use of Radel, resulting in higher scrap levels.
A similar situation to that seen with the processing of Radel also applied to the
processing of Ultem. The processing of this material resulted in a 5.3% scrap level.
Ultem processing also required the use of higher temperatures, ranging in value from
680°F to 740°F. However, the pressures used to process Utem ranged in values from
7,500 PSI to 28,000 PSI. This resulted in the use of a greater pressure range than that
used to process Radel. The use of a greater pressure range led to higher in-mold flow
rates (Reinhold, 1991). A phenomenon such as this can lead to part defects such as splay
48
or contamination. These results tend to support the premise that higher pressures result in
higher scrap levels.
RTP
The highest scrap level as seen in the collection of data for this research resulted
in the use of a material called RTP. When processing RTP, a polycarbonate material, the
recorded melt temperatures ranged from 490°F to 530°F. The mold temperatures used to
process RTP ranged from 70°F to 180°F and the pressures ranged from 4,000 PSI to
17,000 PSI. If the processing of this material is compared to that of Cycolac or Calibre, it
can be seen that the processing parameters are identical. Since this is the case, why does
the processing of RTP result in a very high scrap level, consisting mostly of defects due
to contamination, sink marks, and short shot? Based on the literature review performed
for this research, the processing temperature of RTP or polycarbonate, ranges from a
value of 446°F to 572°F. At processing temperatures just above this range, the material
degrades quite rapidly (Brydson, 1999). The melt viscosity of this material is very high.
During processing, this material's flow path ratios fall in the range of 30:1 to 70:1. These
ratios are substantially less than many of the more general-purpose thermoplastics such as
polypropylene at 175:1 to 350:1, ABS at 80:1 to 150:1, and Nylon 6/6 at 180:1 to 350:1.
The characteristics of RTP just discussed can be used to try and explain the cause
of part defects like contamination, sink marks, or short shot. The high scrap level could
be related to the injection machines used to produce RTP products. Based on the data
collected for this research, most of the time these products were molded using injection
molding machines sized in the range from 200 ton to 400 ton. These are considered high
clamp-force machines at the Short Run facility. These injection molding machines are
49
typically used to produce complicated part designs with complex flow patterns. Due to
the difficulty in moving material through these molds, several types of part defects can
occur. Another reason for high scrap levels could be due to the operator's actions. Again
because of the complexity of some part designs, machine operators often have a difficult
time in identifying the correct processing parameters. This difficulty in setting processing
parameters results in inconsistent cycle times or longer material residence times. These
problems can be the reasons for higher scrap when RTP is used.
Operators
The scrap level associated with each production shift can be explained by relating
them with operators' experience. Most operators working on the A and B lines of 1st shift
have over two years of machine operation experience. These experienced operators are
uniformly distributed throughout the lines. The 1st shift generated a total scrap level of
2.9%. This trend is similar to that predicted by the reading discussed in the literature
review; the more experienced an operator is the less scrap generated. The scrap level of
4.6% associated with 2nd shift was higher than the 3.5% scrap level associated with 3rd
shift. This phenomenon cannot be explained based solely on the experience of each
operator because the operators on 2nd shift and 3rd shift were uniformly distributed with
similar years of experience. Also with each shift on the same production line, the same
machines, processes, and materials were used. The highest scrap level, which was seen
on 2nd shift, can be hypothesized as being a function of something other than operator
experience. By applying practical reasoning to identifying the causes of this problem, it
appears that this higher scrap level could have been caused by outside non-machine
related variables such as time of day, operator alertness, or non-machine related
50
50
responsibilities. These conditions may have an extreme affect on the performance of a 2nd
shift machine operator.
The scrap levels associated to the A-line, B-line, and C-line can be explained
based on machine use and the operators' actions. All A-line injection machines are
smaller in size, from 20 to 40 tons. Most of these machines are relatively new and
modern. The production jobs run on these machines are typically operated in an auto-
function mode, hence consistent cycle times are possible. Also, since these are small
machines, they are used to produce small parts. Due to the smaller sized parts, the flow
patterns are simple and result in less part fill type problems. For these reasons the A-line
scraps levels are low for all three shifts.
Most B-line scrap generation levels can be explained based on machine age and
use. Almost half of the B-line machines are 8 to 14 years old, fairly close to the end of
their life cycle. In addition, the B-line also consists of a vertical injection molding
machine that requires all jobs be operated in a semi-automatic mode. Problems typically
encountered in using this machine can usually be correlated back to the operator. Many
of the jobs produced on the B-line also require that inserts and pick-outs be loaded into
the mold prior to starting a cycle. Therefore, operator experience is a key factor when
problems arise in the B-line.
The C-line scrap level of 5% was better than B-line's scrap level at 7.4%. This
difference in scrap levels can also be explained based on machine age and use. Except for
one 12-year-old machine, most of the machines on C-line are relatively new. These
newer machines are more dependable and require less operator interaction during

51
operation. For these reasons the C-line had a better scrap level rate on all shifts than the
B-line.
The scrap levels associated with the production of the 1st, 2nd, and 3rd shifts of A-
line were 2.9%, 6.8%, and 4.7%, respectively. Because 1st shift of A-line had more
experienced operators than the 2nd and 3rd shifts, operator inexperience was a reasonable
cause for the higher scrap levels seen on the later shifts.
B-line 1st, 2nd, and 3rd shift scrap levels were 4.6%, 9.6%, and 8.0%, respectively.
Some of the differences in scrap levels between shifts can be explained due to the more
experienced operators working on 1st shift, most having more than two years of
experience, and ultimately resulting in the lowest scrap level. The 2nd shift B-line scrap
level was higher than that of the 3rd shift. Again, this phenomenon cannot be explained
based solely on operator experience. Both shifts consist of a similarly uniform
distribution of experienced operators. Since these shifts consist of the same production
lines, machines, processes, and materials, the variation in scrap levels between the B-line
2nd and 3rd shifts may be caused by non process related variables, as presented earlier in
this section.
The scrap levels associated with all of C-line shifts, in chronological order, were
3.5%, 7.5%, and 4.2%. The distribution of operator experience was identical for all shifts.
Therefore, it appears once again that operator experience was not a factor in the scrap
level variances seen between all of the C-line shifts. These variances in all probability
occurred due to non-process dependent variables, as presented earlier.
52
Chapter 5
Conclusion
The generation of scrap is an important problem that must be addressed by
today's businesses. It needs to be controlled for the purpose of lowering costs in an
attempt to gain a competitive advantage in business. Despite several methods currently
used to control scrap generation, a simple way that can help Phillips Plastics-Short Run
control scrap generation is to understand the scrap levels as they relate to injection
molding machines, processes, materials, and machine operators. By understanding the
effects of these process parameters it becomes possible for a production facility to gain
insight into the generation of scrap due to the production conditions for each workstation
as it applies to each job. In this way production facilities can control scrap levels by
making a better informed decisions in the selection of injection machine, process,
material, and operator required to produce a particular job, ultimately minimizing scrap
levels.
This research presented scrap level data associated to the major processing
parameters: injection machine, process, material, and operator. The analysis performed in
this work was subdivided further by examining the scrap levels associated to several
production lines and work shifts. Understanding the reasons for variance in production
lines, shifts, or operators can help Short Run plan for the rise in scrap levels for specific
production jobs. Therefore, it will become possible for Short Run to better adjust
production conditions to minimize scrap generation.
This research analyzes the scrap generated from 100 samples jobs collected at
Phillips Plastics Short Run facility. Most of the research results can be explained based
53
on an understanding of process parameters in regards to injection machine, process,
material, or operator assigned to the production job. Some results, such as the differences
seen between scrap levels from 2nd shift and 3rd shift, and A, B, and C-lines, requires
further study.
Recommendations
Generally, this research identifies the causes for most problems related with the
scrap rates that occur at the Phillips Plastics-Short Run facility based on injection
machines, processes, materials, and operators. Some findings could be refined and
researched further.
The 100 samples collected for use in this research only satisfy basic statistical
analysis requirements, but yield acceptable results for use in this research. For more
accuracy, future research should be performed by collecting more data samples.
Future research should also involve gathering data about mold design. Bad mold
design is another common cause of scrap generation. Including this data in the research
analysis may yield more comprehensive results and help better explain research findings.
Collection of process time variables, such as fill time, pack/holding time, cooling
time, and cycle time, was outside the scope of this research. However, inconsistency in
process time is a common cause of part defects. Including process time in future research
analysis can provide more comprehensive explanations in regards to scrap generation.
Several production jobs required the implementation of secondary operations to
complete part fabrication. These additional operations can lead to an increase in the
amount of part defects. For a more comprehensive study, research should also include
more specific information in regards to this data.
54
References
Beaumont, J.P., Nagel, R., & Sherman, R. (2001). Successful Injection Molding. Hanser
Gardner Publications, Inc.
Brydson, J. A. (1999). Plastics Materials. Woburn, MA: Butterworth-Heinemann.
Johannaber, F. (1994). Injection Molding Machines. Cincinnati, Ohio: Hanser/Gardner
publications, Inc.
Kolz, A. R., McFarland, L. A., & Silverman, S. B. (1998). Cognitive Ability and Job
Experience as Predictors of Work Performance: The Journal of Psychology, 132(5),
539-548
Quiñones, M. A., Ford, J. K., & Teachout, M. S. (2001). The Relationship Between
Work Experience and Job Performance: A conceptual and Meta-Analytic Review.
Personnel Psychology.
Reinhold, V. N. (1986). Injection Molding Handbook. New York, NY: Van Nostrand
Reinhold Company, Inc.
Reinhold, V. N. (1987). Injection Molds and Molding. New York, NY: Van Nostrand
Reinhold Company Inc.
Reinhold, V. N. (1991). Plastics Engineering Handbook. New York, NY: Van Nostrand
Reinhold.
Whelan, A., & Craft, J. L. (1978). Development in Injection Molding _1. Barking, Essex,
England: Applied Science Publishers Ltd.
Appendix A
Scrap Reduction Research Datasheet
Job #:
Collection Date:
Press #:
Item #:
Production Order #:
Dates of Production:
Contamination
Partials
Voids/Bubbles
Sink
Splay
Good
Scrap Total
Shift
Initials
Supervisor's Signature:
Production Manager's Signature:
Material:
Melt Temps:
Mold Temps:
Pressure:
55
555
Appendix B
Press Investigation
For
Scrap Reduction Research
56
56
Press #
Tonnage
Estimated Age
Press #
Tonnage
Estimated Age
A-1
B-5
A-3
B-6
A-4
B-8
A-5
B-9
A-6
B-10
A-7
C-1
A-8
C-2
A-9
C-3
A-10
C-4
A-11
C-5
A-12
C-6
A-13
C-7
A-14
C-8
A-15
A-16
C-9
C-10
B-1
B-2
B-3
B-4
Supervisor's Signature:
Production Manager's Signature:
Appendix C
Initials
Operator Data
For
Scrap Reduction Research
Year(s) of Experience (estimated)
Under 1 yr
1-2 yrs Over 2 yrs
Supervisor's Signature:
Production Manager's Signature:
57

In the range
of melt temperatures under 500°F, the scrap level was 0.8%.

The scrap jumped to a
higher level of 3.9% with the melt temperatures between 500-600°F.

The over all scrap level related with the use of this material was
29
4.6%.

Ultem was another material used often by Short Run. The study shows that the
over all scrap level related with using this material was 5.3%. Most scrap problems
occurred due to splay. The next problem occurred due to contamination scrap level.
Void/Bubble and burn/streak scrap levels were much lower than splay and contamination
scrap levels. For this material, scrap levels due to sink marks and partial fill were very
low. Therefore, splay and contamination should be closely monitored when using Ultem.

Table 4 shows that the over all scrap level associated with using Cycolac was
2.5%. The most common scrap problem presented with using this material proved to be

At higher mold temperatures (200°F and up) the
scrap level was 2.9%.

As Figure 5 shows, at the lower range of pressures (under 10,000 PSI), the scrap
level was very high at 9.3%. At the mid-range of pressures (10,000-20,000 PSI), the
scrap was lower at 3.7%. The process at higher pressures, 20,000 PSI or higher, resulted
in a scrap level of 4.8%. In general, the scrap level was lowest at pressures of 10,000PSI
to 20,000PSI. The processes that require higher pressures produce higher level of scrap.
However, at a lower pressure (under 10,000 PSI) the scrap level also becomes very high.
The five most commonly used materials for this research were Calibre, Radel,
Ultem, Cycolac, and RTP. Calibre was the most commonly used material in the data
collected for this research. Table 1 show that the over all scrap level associated with
using this material was 3%. The contamination level related with this material resulted in
the highest specific scrap level. The scrap level due to burning, void/bubble, and splay
were also monitored. Scrap levels due to partial fill were very low using this material,

The scrap percentage reduces to about half (at 4.7%) in the mid-range
of mold temperatures (100 °F -200°F).

At lower mold temperatures (under 100°F), the scrap level reaches a very
high level of 8.6%.

The over all scrap level related with using RTP is presented in Table 5, and was
found to be 9.3%. The table also shows the biggest problem was scrap due to
contamination. Sink marks and partial fill scrap levels should also be considered. Splay,
bubble, and burning scrap levels were rarely problematic when using this material.
Therefore, most scrap reduction efforts should be focused on contamination during the