BS 5701-1
BS 5701-1
14 March 2004
ICS 03.120.30
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BS 5701-1:2003
Contents
Page
Committees responsible Inside front cover
Foreword ii
1 Scope 1
2 Normative references 1
3 Terms, definitions and symbols 1
4 Qualitative (attribute) data fundamentals 1
5 Business process focus and management 7
6 Supporting techniques for effective process control and
performance improvement 9
7 Relationship with Six Sigma initiatives 15
8 Typical case study 16
Annex A (informative) Base data for case study of Clause 8 25
Bibliography 27
Figure 1 — Different classes of data 3
Figure 2 — Process control, capability estimation and improvement
sequence 4
Figure 3 — Control chart for assembly of men’s briefs 6
Figure 4 — Basic process model 10
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Foreword
BS 5701-1 demonstrates the business benefits, and the versatility and usefulness
of a very simple, yet powerful, pictorial control chart method for monitoring and
interpreting qualitative data. This is done in a practical and largely
non-statistical manner. BS 5701-1:2003 partially supersedes BS 5701:1980 and
BS 2564:1955 and all four parts of BS 5701 together supersede BS 5701:1980 and
BS 2564:1955, which are withdrawn.
This qualitative data can range from overall business figures such as percentage
profit to detailed operational data, such as percentage absenteeism, individual
process parameters and product/service features. The data can either be
expressed sequentially in yes/no, good/bad, present/absent, success/failure
format, or as summary measures (e.g. counts of events and proportions). For
measured data control charting, refer to BS 5702-1.
The focus is on the application of control charts to monitoring, control and
improvement. The roles of associated diagnostic, presentation and performance
improvement tools, such as priority (Pareto) analysis, cause and effect diagrams
and flow charts are also shown.
Its aim is to be readily comprehensible to the very extensive range of prospective
users and so facilitate widespread communication, and understanding, of the
method. As such, it focuses on a practical non-statistical treatment of the charting
of qualitative data, presenting examples of construction and application using a
simple pictorial approach.
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Summary of pages
This document comprises a front cover, an inside front cover, pages i and ii,
pages 1 to 27 and a back cover.
The BSI copyright notice displayed in this document indicates when the
document was last issued.
1 Scope
BS 5701-1 describes, in lay terms, the uses and value of pictorial control chart methods for enhancing the
presentation and general understanding of qualitative (attribute) data arranged in a meaningful sequence.
It also illustrates the supporting roles of associated business improvement tools. These include process
modelling, flow charting, prioritizing (Pareto analysis) and cause and effect diagrams.
2 Normative references
The following referenced documents are indispensable for the application of this document. For dated
references, only the edition cited applies. For undated references, the latest edition of the referenced
document (including any amendments) applies.
BS EN ISO 9000:2000, Quality management systems — Fundamentals and vocabulary.
BS ISO 3534-1, Statistics — Vocabulary and symbols — Part 1: Probability and general statistical terms.
BS ISO 3534-2, Statistics — Vocabulary and symbols — Part 2: Applied statistics.
computers status
communications clarity, timeliness
Type of data
discrete continuous
(attribute) (measured)
(qualitative) (quantitative)
See BS 5702
count of classified into
events (e.g. categories
nonconformities) (e.g. good/bad)
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4.3 Principles, objectives and rationale of the control charting of qualitative data
4.3.1 Overview
Mention of the word statistics invokes a feeling of apprehension in many people. However, everyone should
positively respond to, understand and adopt the primary concepts of “statistical thinking”. These are as
follows:
1) All work occurs in a system of interconnected processes.
2) Variation exists in all processes.
3) Elimination of special cause variation produces process stability and predictability.
4) Reduction in common cause variation is the key to continual improvement.
The first concept highlights that “statistical thinking” should not be confined to a specific function of an
organization. It is applicable across the whole spectrum of business activity.
The second concept brings out that variation is present in almost everything. Its existence provides
opportunities for better process control and for process performance improvement.
The third and fourth concepts stress the need to clearly distinguish between the variation due to
“special causes” and that due to “common causes”. The reason for this is that they give rise to two quite
different types of action. A special cause is a sporadic source of variation that demands specific action to
restore the status quo. A common cause, on the other hand, is an endemic source of variation that is always
present, as it is inherent to the process. A reduction demands fundamental changes to the process.
The elimination of special causes brings a process back under control. The process performance or
capability is then stable and predictable. A stable process might, or might not, provide the desired
performance. A reduction in common cause variation improves process capability or performance.
A control chart is the tool used to differentiate between “special causes” and “common causes”. Hence the
control chart is a key operational tool in the application of “statistical thinking”.
By its very name, a primary role of a control chart, in an operational sense, is to control; namely to inhibit
change. The removal of adverse special cause variation to bring a process back into control does not actually
improve the process: it only returns it to its original state.
It should be borne in mind, too, that a special cause can be adverse or beneficial. Suppose a supervisor
stands in momentarily for an operator in a process and a special cause is indicated on a fault chart. The
special cause could be a single reading above the upper control limit indicating an adverse change.
Alternatively, it could be a single reading below the lower control limit indicating a beneficial change. The
reaction to the two types of special causes would be quite different.
This focus on control, however, should not blind one to the fact that often the objective, in an overall sense,
is to improve process performance by inducing change. Such betterment, through common cause reduction
does not necessarily have to await special cause removal. However, the prior removal of special causes gives
rise to a stable process and so permits a quantitative prediction of process capability. The generic control
and improvement sequence is shown in Figure 2.
A significant improvement in process performance is evidenced in a control chart by an “out of control”
situation, as is a significant deterioration. Hence the control chart has an in-built statistical test of
significance for both improvement and deterioration.
Select
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quality
characteristic
yes Is process no
stable?
Priority Is special
no for no
cause
improvement? adverse?
yes yes
Reduce Eliminate
common special
causes cause
— common cause variation: a source of variation that is inherent in a process over time.
When no special cause is present, the process is considered to be stable. It is then said to be in a state of
statistical control. The capability of a stable attribute process can be calculated directly from the centre-line
of the control chart. When a special cause is present, the process is said to be “out-of-control” and needs to
be brought back under control.
These process states are readily determined from an attribute control chart. The attribute control chart is
essentially a simple run chart with two added features, a centre-line and one or two control limits. The
centre-line on an attribute control chart is normally the historical mean of the feature plotted. The control
limit, or limits are lines on a control chart placed about the centre-line to evaluate whether, or not, the
process is in a state of control. Typical criteria for assessing whether a control chart indicates an
“out-of-control” situation are:
a) any point outside of the control limits;
b) any run of seven consecutive points above or below the centre-line;
c) any run of seven consecutive points up or down;
d) any obvious non-random patterns (based on technical and operational knowledge of the process).
4.3.4 Case study
Figure 3 shows a specific example of the use of an attribute control chart in process improvement. It relates
to an underwear making-up (assembly) process.
20
15 Oil leak
10
5 UCL
0
Summarizing, Figure 3 illustrates that an attribute control chart is no more than a simple run chart with
additional guidance in interpretation in the form of centre-lines and control limits. It is easy to create and
yet it provides direct visual answers to the three key questions one should be asking of every significant
process in any organization, namely:
i) Is the process in control?
ii) What is the performance of the process?
iii) Is there evidence of improvement in performance?
An additional point is that many control systems include reaction procedures only for adverse
“out-of-control” situations. It is illustrated here that a process also needs to go “out-of-control”, in the
favourable sense, for an improvement in performance to occur.
others on whom they rely (e.g. suppliers of product and information) and support (e.g. customers), share a
common understanding of the nature of the process and the impact of its performance on both the
processor, customers and input suppliers.
5.2.3 Establish responsibilities
Responsibilities should be defined as follows.
— Ensure that there is someone in charge of the process.
— Ensure that individual responsibilities are established for process control and team responsibilities
for process performance improvement.
The primary objectives at this step are to:
a) identify an overall process owner who is ultimately accountable for the process and who manages the
process across functional and organizational interfaces;
b) define roles and responsibilities of everyone involved in process control and process improvement;
c) ensure significant interface interests are represented;
d) make it quite clear who is responsible for initiating and managing reaction to out-of-control signals
and process improvement projects.
5.2.4 Define and establish process controls
Ensure that controls are established to ensure stability of the process and to enable assessment of the
degree to which the process is satisfying customer expectations and business objectives. This involves the
definition of:
a) what to control. Identify control subjects that are relevant. Use selective emphasis. Separate the vital
few from the trivial many. For example, key accounts might have preferential treatment; bottlenecks
might have special consideration and characteristics generally that receive controls appropriate to their
criticality;
b) dominant influencing factors. Although a process can be subjected to many sources of variation often
a few sources predominate. Once located these predominant factors provide the basis for economic and
effective control. Dominant factors to look out for include:
i) information dominant: where non-conformities and other undesirable events arise from frequent job
and requirement changes;
ii) time dominant: where process performance changes with time;
iii) set-up dominant: where the characteristic is highly reproducible once correctly set up;
iv) process dominant: where the process output is highly dependent on certain process parameters;
v) processor dominant: where the process is highly dependent on the skill, care and attention of the
people performing the task.
c) the level of control. Choose the appropriate level of control. Examples are:
i) automatic control, e.g. thermostatic control of temperature, laser scanning of fabric for faults during
production, traffic lights and sleeping policemen (humps) in the road;
ii) self-regulation by the person performing the task (e.g. the car driver who drives naturally on the
proper side of the road and obeys traffic signals);
iii) independent check/inspection/test/audit;
iv) information control where selected personnel are provided with reports of errors and absenteeism.
Whatever the decisions made in terms of items a) to c) the methods of process control recommended in this
standard have universal applicability to attribute data characteristics. The control charts described are
easy to construct and interpret. They express a common language readily understandable throughout the
world.
5.2.5 Assess and improve process performance
Achieving and maintaining stability of a process is essential. Control, too, in the sense of meeting budgets,
quota and specifications is equally important. But holding rejects at a budgeted level of, say, 7 %,
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particularly if this loss exceeds the profit margin, obviously does not make good business sense.
The conclusion is that a preoccupation with control should not blind one to the needs, expectations and
opportunities for process performance improvement.
A number of thought stages are involved in successful process improvement projects. These include:
i) understanding the extent to which process performance affects customer (internal and external)
satisfaction and process cost;
ii) appreciating the need to achieve a stable process by applying appropriate controls before assessing
process performance;
iii) estimating “first-run” process performance for individual process stages and for the process as a
whole;
iv) prioritizing opportunities for improvement;
v) achieving and sustaining improved levels.
Controls
Inputs Outputs
PROCESS
Resources
NOTE 1 Inputs are materials and/or data that are transformed by the process to create outputs.
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NOTE 2 Outputs are the result of transformation of inputs. Outputs can include acceptable customer wants, unacceptable process
wants, waste and process information.
NOTE 3 Controls are regulators and/or influences on the process. Controls embrace procedures, methods, control plans, standards
and legislation.
NOTE 4 Resources are people, equipment, material, space, etc. that are not transformed into output.
An application of a typical basic process model is shown in Figure 5.
work schedule
work instructions
change documents
new parts
updated
items to change ACTION equipment
installed equipment DESIGN information
CHANGE
surplus parts
tools
test equipment
personnel
Figure 5 — Application of the basic process model to the actioning of a product design change
A process can relate to a complete organization in macro format; to a single task in micro format
(as in Figure 5) or to a set of several processes in cascade form (as in Figure 6).
Customer Customer
Outputs Inputs Outputs
Inputs
Supplier Supplier
monitoring and the strategy of prevention possible with in-process monitoring. Examples of post-process
monitoring, namely “after the event” product characteristic monitoring, include number and types of fault
at each stage, and post-process stage inspection information. Examples of in-process monitoring, namely
“during the event” process parameter monitoring, include ram velocity, transition pressure, cooling time,
pin positions on extrusion, proximity switch position, router choice, extruder type and trimming blade
status.
Whilst Figure 7 relates to a manufacturing process, the same approach is applicable to any process in any
organization.
ram velocity
extruder rpm transition press
no of pins cooling time router calibration,
pin positions proximity sw. pos. choice R & R capability
vinyl pellets,
moisture extrude prod. rate,
nos & types
puck puck of fault
cycle time,
press nos & types
puck discs
with of fault
flash
trim prod. rate,
disc nos & types
of fault
discs
inspection info
measure
inspected discs
scrap = 3 scrap = 2
i/p =100 o/p = 97 i/p =100 o/p = 100 i/p =100 o/p = 98
Process Process Process
1 2 3
rework = 2 rework = 3
Figure 8a) — Illustration of the calculation of logistic capability and first run capability of a
process stage
·
good output
NOTE 1 Logistic capability = -------------------------------- × 100 % .
input
(N – W)
NOTE 2 First run capability (FRC) = --------------------- × 100 %.
N
N = number of items entering the process.
W = waste = number of items that are not processed right first time whatever the ulitmate disposition (e.g. reworked, scrapped).
In Figure 8b), the principles of Figure 8a) are applied to the integrated multistage process illustrated
in Figure 7.
rework = 5 rework = 6
Stages 1 2 3 4
Logistic
capability 90/100 = 90 % 87/90 = 96.7 % 82/87 = 94.3 % 74/82 = 90 %
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First run
capability 90/100 = 90 % 82/90 = 91.1 % 76/87 = 87.4 % 74/82 = 90 %
Figure 8b) shows that whilst stage capabilities look quite respectable, being in the 90 %’s, overall
capabilities of the integrated multistage process are much less attractive. It also shows that the logistic
capability, at 74 % overall, is much more optimistic than the actual first run capability, at 63 % overall.
These examples illustrate the value of the use of overall first run capability to identify process
improvement opportunities, to exploit these, and to verify the effectiveness of any changes made to the
process. They also show the need for an overall management perspective when dealing with multistage
processes rather than the narrow stage view that can be taken by discrete functional departments.
6.3 Pareto analysis
Pareto analysis is a simple graphical technique for displaying the relative importance of features, problems
or causes of problems as a basis for establishing priorities. It distinguishes between the “vital few” and the
“trivial many” and hence focuses attention on issues where maximum quality improvement is secured with
the minimum effort. An example is shown in Figure 9.
100 60
Number of occurences
80 50
40
60
Percent
30
40
20
20
10
0 0
l run
s rs es on pra
y pits
pee blis
te tch ati un s
Defect: range g s and scra flot overs g
o sa
Count: 24 17 8 5 5 2 2
Percent: 38.1 27.0 12.7 7.9 7.9 3.2 3.2
Cum.%: 38.1 65.1 77.8 85.7 93.7 96.8 100.0
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NOTE The faults are arranged in order of incidence in Figure 9. However, other measures of meaningfulness, such as costs, are
sometimes used. For instance, one fatal accident insurance claim can be of much greater significance than dozens of claims for minor
injuries
small
squeeze
pressure ladle size
mould
size cycle rate of large
time pour
blow
pressure mould pour innoculation
hardness temp.
cracks in
BLEND MOULD MELT POUR brake disc
casting
% active
clay
12 % 70/30
Figure 10 — Process cause and effect diagram for cracks in a brake disc casting
Table 2 — Relationship between Sigma value, non-conformities per million opportunities and
percentage yield
Six Sigma Non-conformities (or events) per million Yield
Sigma Value opportunities %
1 691 462 30.8
2 308 538 69.1
3 66 807 93.3
4 6 210 99.4
5 233 99.98
6 3.4 99.999 7
This standard provides methods to support the Six Sigma continual improvement initiative in respect of
attribute data. However, the principal purposes of this standard are to engender a mindset and provide
methods that support the targeting on:
1) “preferred value or condition”, rather than something that is “just acceptable” by proposing an offset
or relief from a target condition.
2) zero fault rates, rather than an arbitrary finite value.
70
60
UCL
50
Number of faults
40
Mean
30
20 LCL
10
0
0 10 20 30 40 50 60
Day
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100
80 1 500
Number of occurences
60
Percent
1 000
40
500
20
0 0
SS op s ds egs fly s rs
Defect: Lap ar lo ban de l lose End othe
B Insi C
100
80 1 500
Number of occurences
60
1 500
Percent
40
500
20
0 0
en dy lie a e e e e t et n m rs
Defect: Su Dore Man Rosa Rit Juli Jan Jun Su Pa Jan Daw Pa Othe
30
Number of faults 25
20
Doreen
15
UCL
10
Mean
5
0
0 10 20 30 40 50 60
Day
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Figure 14 — Doreen lapping side seams (5.3 faults per day); Total 275 faults
(15 % of total faults)
10
Jane (2.1/day)
Number of faults
UCL
Mean
0
0 10 20 30 40 50 60
Day
25
20
Rita (5.5/day)
Number of faults
15
10 Sue (2.8/day)
0
0 10 20 30 40 50 60
Day
The tentative initial conclusions drawn on lapping side seam performance is that this is the most difficult
operation in the assembly of trousers. Even the most skilled machinists, Sue and Jane, suffer a
between 2 % and 3 % fault rate. Sue left the company early in the project and Jane followed later. The fault
rates borne by Doreen and Rita are about twice that of the other two.
8.2.3.3 Bar loops
There is a big contrast between the performance of the two machinists barring the trouser loops as shown
in Figure 17 and Figure 18. Brenda is seen to be inherently capable of a virtually fault-free performance.
Figure 17 shows that Su initially produced some 8.8 faults per day compared with that of Brenda’s 0.19
faults per day. This represents a difference of some 46 times. Following retraining/recalibrating regarding
the standard required, Su’s performance is seen to improve from 8.8 faults per day to 0.33 faults per day.
Apart from the odd special cause concern, Su is now also inherently capable of a zero defect performance.
The results from this situation should be sufficient to alert management to the potential for a major
breakthrough in business performance. It should be used as an exemplar of what can, and should, be
achieved across this and similar lines in the business.
30
25
Faults per day
20 Su (8.8/day)
UCL
15
10 Su (0.33/day)
after calibration
5
UCL
0
0 10 20 30 40 50 60
Day
1 Brenda (0.19/day)
0
0 10 20 30 40 50 60
Day
8.2.3.4 Bands on
Mandy is the only machinist on this line putting the bands on. She is looked upon as being a very good
operator. However, the control chart in Figure 19 indicates three poor, but quite different, performance
levels. An initial performance of 4.9 faults/day is followed by a period of 3.1 faults/day that in turn is
succeeded by some 9 faults/day. A similar situation exists on a different line. It appears that shading
(variations in colour shade) of the bands, which are supplied in batches, may be a major contributor to the
variation in, and sub-standard performance of, this operation. This is to be investigated.
20
15
Mandy
Faults per day
10 9.0
4.9
5
3.1
0
0 10 20 30 40 50 60
Day
10
9 UC L
8 Rosalie
7
Number of faults
6
5
4 Mean
3
2
1
0
0 10 20 30 40 50 60
Day
Dorry
2
Number of faults
Delia
1
0
0 10 20 30 40 50 60
Day
15
Shirley
0
0 10 20 30 40 50 60
Day
5
Janet (1.5/day)
Faults per day
0
0 10 20 30 40 50 60
Day
5
Jean (1.8/day actual)
4
Faults per day
[1.2/day achievable]
3
0
0 10 20 30 40 50 60
Day
Annex A (informative)
© BSI 31 October 2003
BS 5701-1:2003
.. Dorry
Total 37 19 29 55 24 19 29 30 51 48 31 21 31 47 53 42 24 36 42 50 62 22 53 37 39 43 19
25
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Table A.1 — Base data for case study of Clause 8 (continued)
26
BS 5701-1:2003
Process Machinist Day
Yokes Teresa 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 1 0 0 0 0 12
Bk Seams Glen 1 0 0 0 0 0 0 0 0 0 0 1 1 1 3 0 3 1 0 0 4 4 0 0 1 49
Roll Pkt Dawn1 0 0 1 2 3 4 16 3 0 0 1 1 0 1 1 0 0 0 0 1 0 0 0 0 1 52
Bind Pam 2 0 2 1 1 1 2 2 0 1 2 0 1 2 2 1 0 0 1 2 1 2 0 0 1 52
Serge Fly Pat 0 0 0 0 0 0 0 0 1 1 1 0 1 0 0 0 3 3 2 0 8 1 0 3 1 63
Close Fly Jean 3 1 0 2 1 2 0 2 1 1 2 0 1 2 2 0 2 0 3 1 0 1 2 0 2 92
.. Janet 2 2 0 1 2 1 2 2 3 1 2 4 1 2 3 1 1 0 0 0 0 0 0 0 0 60
.. Shirley 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 2
.. Dawn2 15 7 0 0 0 0 1 0 0 0 23
Lap SS Doreen 3 2 3 3 2 3 4 3 6 3 5 2 8 3 0 6 3 25 17 5 15 13 5 6 5 275
.. Sue 75
.. June 3 2 2 7 4 0 3 3 2 2 0 1 2 2 0 1 3 9 3 0 2 4 2 5 4 83
.. Rita 2 3 1 2 2 2 6 6 3 3 3 5 2 4 3 6 4 5 11 7 12 11 5 7 23 138
Bands Mandy1 3 2 10 2 4 2 5 1 6 3 5 3 4 3 4 3 4 1 2 0 11 6 11 4 13 250
Ends Julie 3 0 1 4 2 4 2 3 2 2 1 0 0 1 0 4 2 7 3 1 8 6 3 0 1 108
.. Sharon 0 0 0 0 0 0 0 0 0 0 16
Barr Loops Su 14 6 5 10 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 1 6 280
.. Brenda 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 10
Fly Tack Jeanet 0 0 0 0 0 0 0 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 1 0 5
Zip Stop Mandy2 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
.. Heather 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 3
.. Jeanet 1 0 0 0 0 0 0 0 0 0 0 0 0 0
0 0 0 0 0 0 0 0 0 0 0 1
In Legs Rosali 0 7 3 2 3 3 6 5 0 3 1 7 4 0
2 3 0 1 2 1 2 3 6 1 2 171
.. Delia 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 3
.. Dorry 0 0 0 0 0 0 0 0 0 7 0 7
Total 37 25 28 36 24 22 46 31 24 20 23 24 25 21 20 40 32 52 44 18 64 52 34 35 60 1 830
© BSI 31 October 2003
BS 5701-1:2003
Bibliography
British Standards
BS 5701-2, Guide to quality control and performance improvement using qualitative (attribute) data —
Part 2: Fundamentals of standard attribute charting for monitoring, control and improvement.
BS 5701-3, Guide to quality control and performance improvement using qualitative (attribute) data —
Part 3: Technical aspects of attribute charting: special situation handling.
BS 5701-4, Guide to quality control and performance improvement using qualitative (attribute) data —
Part 4: Attribute inspection performance control and improvement.
BS 5702-1:2001, Guide to statistical process control (SPC) charts for variables — Part 1: Charts for mean,
median, range and stardard deviation.
Other publications
[1] TRUSCOTT, W. Six Sigma: Continual improvement for businesses. Butterworth-Heinemann: 2003.
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