| Literature DB >> 35607483 |
Radosław Drozd1, Radosław Wolniak2, Jan Piwnik3.
Abstract
The main aim of the article is to present two new innovative concepts of reliability of a functioning manufacturing system in the process of making bread in small-scale bakeries. Reliability is understood as one of the representations of an operator acting on specific streams in time to to t. One of these represents the global reliability of a system as a function of parallel action of all the streams of the system in time to to t and is denoted as Pg (t). The second representation of reliability is a scalar value, Pss It shows a new function of global reliability of a manufacturing process as a product of system stream reliability. In order to plot the flow of the manufacturing process's global reliability function, we need to perform detailed calculations, computations, and analysis of the differences of individual values in real time, as well as plan an algorithm of the flow of system streams. This needs a lot of effort, translating however, to a detailed picture of the process. In the analysed example, measurements and research revealed an important increase of the value of reliability in a transition from a traditional to a robotised bakery. The article also presents a new concept of the reliability of a technological process, based on the analysis of relations of elements of the following streams: energy, matter, information, time, and finances. It shows the method of specifying streams and the method for defining the reliability of important and supportive relations. Important relations between stream elements are defined as having the reliability value of one in time. Supportive relations bear the reliability within a continuum between zero and one. Important relations are designated based on research, experience, and knowledge. Stream systemic reliability Pss is a scalar value, i.e. a number from the continuum between zero and one. The Pss value characterises failure-free operation of the whole system. Its average value in the normative time tn expresses the efficiency of the manufacturing system. The value Pss is a quotient of the number of important relation and the sum of important and supportive relations. The formula for Pss shows the method of optimising the process through the increasing of the number of important relations between the input stream components. The concept has been applied to study the efficiency of operation of a small-scale bakery. Systemic analysis of a bakery allows for important increase in the reliability of baking bread if robotisation has been implemented. The concept of systemic-stream reliability Pss may be applied to analyse the efficiency of any technological process and optimisation of any manufacturing process.Entities:
Keywords: Analysis of relations streams; Bread baking; Manufacturing process reliability; Quality
Year: 2022 PMID: 35607483 PMCID: PMC9117986 DOI: 10.1007/s11135-022-01408-7
Source DB: PubMed Journal: Qual Quant ISSN: 0033-5177
Fig. 1Structure of the system of the analysed bakery.
Source: Own elaboration
Fig. 2Spatial distribution of manufacturing facilities and halls before the robotisation process in the analysed bakery.
Source: Own elaboration on the analysed bakery
A list of rooms, machines, and facilities in the analysed bakery
| Symbol | Room | Symbol | Machine |
|---|---|---|---|
| 1p | Dressing room | 1 m | Bread roll manufacturing line |
| 2p | Mess | 2 m | Working table |
| 3p | Production hall No. 1 | 3 m | Mixer |
| 4p | Production hall No. 2 | 4 m | Bread manufacturing line 1 |
| 5p | Production hall No. 3 | 5 m | Frier |
| 6p | Confectionery | 6 m | Packing machine |
| 7p | Distribution space | 7 m | Lamination line |
| 8p | Warehouse 1 | 8 m | Confectionery beater |
| 9p | Warehouse 2 | 9 m | Working table |
| 10p | Washing room | 10 m | Dough roller |
| 11p | Dough room | 11 m | Thermal-oil ovens |
| 12 m | Thermal-oil ovens | ||
| 13 m | Mixer | ||
| 14 m | Gas stool | ||
| 15 m | Bread manufacturing line 2 | ||
| 16 m | Working table | ||
| 17 m | Bread slicer | ||
| 18 m | Working table | ||
| 19 m | Slicer | ||
| 20 m | Slicer | ||
| 21 m | Clipping machine | ||
| 22 m | Material cooler | ||
| 23 m | Material cooler | ||
Source: Own work on the analysed bakery
Energy stream elements (fragment)
| Designation | Element number (i) | Name of element | Type of energy |
|---|---|---|---|
| 1 | Spiral mixer | Mechanical | |
| 2 | Proofing room | Thermal | |
| 3 | Thermal-oil oven | Natural gas |
Source: Own elaboration on the analysed bakery
matter stream elements (fragment)
| Designation | Element number (j) | Name of element | Type of matter |
|---|---|---|---|
| 1 | Wheat flour | Powder | |
| 2 | Water | Liquid |
Source: Own elaboration on the analysed bakery
information stream elements (fragment)
| Designation | Element number (k) | Name of element | Type of information |
|---|---|---|---|
| 1 | Material storage instruction | Instruction | |
| 2 | Material measurement | Measurements |
Source: Own elaboration on the analysed bakery
time stream elements (fragment)
| Designation | Element number (l) | Name of element | Type of time |
|---|---|---|---|
| 1 | Silo operation time | Technological time for the machine(s) | |
| 2 | Bread cooling | Technological time for the product |
Source: Own elaboration on the analysed bakery
finance stream elements (fragment)
| Designation | Element number (m) | Name of element | Type of finances |
|---|---|---|---|
| 1 | Flour unit costs | Material costs | |
| 2 | Proofing room work | Machine working cost |
Source: Own elaboration on the analysed bakery
Fig. 3Flow of the global manufacturing reliability function for a traditional bakery
Source: Own work
Fig. 4Flow of the global manufacturing reliability function for a robotic bakery.
Source: Own work