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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
181

Analýza podnikových procesů ve firmě Rekstan, spol. s.r.o.

Procházka, Marek January 2011 (has links)
No description available.
182

Modelování podnikových procesů a inovace informačního systému ve společnosti BS vinařské potřeby s.r.o.

Ševčík, Ondřej January 2011 (has links)
No description available.
183

Procesní zlepšování ve společnosti DHL Express Czech Republic s.r.o

Vyklický, Martin January 2011 (has links)
No description available.
184

Conversion of a batch biodiesel plant from homogeneous to heterogeneous catalysed process: modelling, optimisation and techno-economic analysis

Mbadinga, Monique Anais Bakoussou January 2015 (has links)
Most biodiesel plants operate batch-wise using homogeneous alkali catalysts. Recently, several heterogeneous catalysts have been suggested in literature, as they have shown potential for overcoming most of the challenges associated with the application of homogeneous catalysts. Previous published techno-economic comparisons of the two technologies on large-scale processes located in the developed world, have revealed the economic superiority of heterogeneously catalysed processes. Hence, prospect exists for current homogeneously catalysed process plants to be converted to heterogeneously catalysed ones. The objective of this research was to investigate the actual cost benefit of converting a small-scale batch biodiesel plant from homogeneous to heterogeneous catalysed process. For this purpose, a small-scale batch biodiesel plant located in South Africa was taken as the base case homogeneous process. Aspen Batch Process Developer® software was used to perform the process simulations. The homogeneous process was converted to the heterogeneous one and results from process simulation were used to evaluate the economics of both processes, which were compared in terms of fixed capital cost, total manufacturing cost and profitability indicators. During economic evaluation, two types of cost factors were used: one prevailing in developed world and the other one relevant to South Africa. The sensitivity analysis of both processes was further performed in order to investigate the impact of some uncertain parameters on their profitability. Finally, a debottlenecking study was carried out. Results obtained from this study showed an increase in the annual throughput of biodiesel as well as significant savings in the total capital cost for the heterogeneous catalysed process relative to the homogeneous one. As regards the estimation of the total unit manufacturing cost of biodiesel, significant differences arose when using the two types of cost factors. Results of economic analyses estimated using cost factors relative to South Africa suggest an increase in the unit manufacturing cost of biodiesel while using the developed world’s cost factors suggests the opposite. This is due to the higher raw material and energy requirement for the CaO process, while knowing that the direct costs are a bigger proportion of the manufacturing costs estimated using the South African cost factors. Profitability and sensitivity analyses only provided positive results when estimated using the South African cost factors. In all cases, the heterogeneous catalysed process was found to be more promising than the homogeneous one over the prescribed project life. The study showed the importance of using cost factors relevant to a particular economic environment during techno-economic assessment of a process. It was also shown that there are economic benefits when replacing settling with centrifugation in biodiesel production processes. In summary, this thesis makes some important contributions. It presents the first process simulation for biodiesel production using Aspen Batch Process Developer® software and thereby proposes a methodology that is currently scarce in the literature. It also reports the first techno-economic analysis applied to the biodiesel field in South Africa and provides a preliminary insight to owners of biodiesel plants as regards the decision to convert or not their homogeneous catalysed plant to heterogeneous one.
185

Aplicação do Process Mining na Auditoria de Processos Governamentais

PESTANA, L. F. 06 December 2017 (has links)
Made available in DSpace on 2018-08-01T23:38:03Z (GMT). No. of bitstreams: 1 tese_10969_Dissertação Luciana França_Versão Final.pdf: 2442120 bytes, checksum: c6bc5141d2f33e637a2a6eb80e448216 (MD5) Previous issue date: 2017-12-06 / A auditoria de processos de negócios é um tema de relevância crescente na literatura. No entanto, técnicas tradicionais e manuais demonstram-se insatisfatórias ou insuficientes, visto que as mesmas são custosas, podem ser tendenciosas e passíveis de erros, além de envolverem grande quantidade de recursos temporais, humanos e materiais. Nesse sentido, o presente estudo vem demonstrar como a técnica de process mining pode ser utilizada, de forma automática, na auditoria de processos governamentais, a partir de um sistema de informação e de uma ferramenta de mining denominada ProM. A partir de técnicas de verificação de conformidade, realizou-se a comparação entre os processos reais e seus respectivos modelos oficiais de uma organização governamental. Os resultados obtidos demonstram algumas divergências entre eles, e indicam que a técnica pode ser utilizada como um meio auxiliar na realização de auditoria de processos de negócios.
186

My body My tool - Don't fucking tell me what to do!

Silins, Lija January 2017 (has links)
No description available.
187

The Consequences of Implementing Statistical Process Control

Sower, Victor E. 08 1900 (has links)
This study evaluated the changes which occur in manufacturing organizations in the plastic molding industry which implement statistical process control (SPC). The study evaluated changes in product quality, consistency, cost, changes in employee attitudes, and changes in the organization structure which occur after the implementation of SPC. The study was conducted in two phases. Phase 1 consisted of an exploratory field study of a single manufacturing company. Phase 2 consisted of a field survey of three manufacturing companies in the same industry. An unexpected opportunity to evaluate the differences in effects of successful and unsuccessful SPC implementations occurred during the field survey. One plant, whose management assessed their SPC program as being unsuccessful, reported no economic or quality benefits from SPC. Neither did this plant report any changes in the attitudes or behavior of their employees. Neither of these findings was surprising since this plant was the only one of the four study plants which implemented SPC as a quality control program with no participation from the production department. The three plants whose management assessed their SPC programs as being successful reported reduced product variation and a decrease in the proportion of defective product produced as a result of SPC. No consistent evidence was found concerning a reduction in the material required per product resulting from SPC. No consistent evidence was found linking changes in employee attitudes and behavior to the implementation of SPC. The field study found a significant change in the employees1 attitudes toward management but no change in their attitudes toward the company. The field survey found no evidence of change in either dimension. Evidence was found for a change to a more organic structure during SPC training and to a more mechanistic structure during SPC implementation. The final form of the organization was more organic than before SPC. No consistent evidence was found for an increase in hierarchical levels or a reduction in the spans of control within the production departments as a result of SPC. All three of the plants with successful SPC programs increased the size and authority of their technical support staffs as a result of implementing SPC.
188

Factors Contributing to Business Process Reengineering Implementation Success

Dell'Aquila, Mary Elizabeth 01 January 2017 (has links)
Organizational leaders continue to use business process reengineering (BPR) as a process improvement methodology even though BPR implementations have had low success rates. To increase BPR success rates, organizational leaders must understand what specific factors contribute to successful BPR implementations. Grounded in Lewin's field theory, the purpose of this nonexperimental, cross-sectional study was to examine the impact of gender and education on BPR. Data collection consisted of nonprobability convenience sample of 122 members from the professional networking website LinkedIn and the professional organizational website American Society for Quality. Data were gathered from a 6-point Likert-type scale survey instrument based on Hammer and Stanton's pre-identified BPR failure factors. The MANOVA results indicated no significant gender, education, or gender and education interaction effect on a linear combination of perception of BPR success factors, F (33.00, 318.00) = .591, p > 0.05, partial eta squared =.058. The results of this study might contribute to social change by helping organizational leaders understand factors that do not appear to be related to successful BPR implementations. The elimination of these factors could allow organizational leaders to focus on other factors for successful BPR implementations. Successful BPR implementations might lead to increased organizational profits, which could allow organizational leaders more opportunity and increase corporate social responsibility, all of which may directly affect the quality of life in a community.
189

APPLYING COGNITIVE PROCESSES TO FRANCHISEES: THE USE OF ENTREPRENEURIAL MEASURES TO STUDY FRANCHISEE RESPONSE TO CONSTRAINTS

MOORE, TERRENCE W. 30 June 2003 (has links)
No description available.
190

Dynamic Simulation and Control of a Hybrid Coal Gasifier / Steam Methane Reformer System

Seepersad, Dominik 22 April 2015 (has links)
<p>Polygeneration plants are proposed as an attractive solution to today’s challenging economic and political climate, whereby fossil fuels (e.g.: coal, natural gas) can be co-processed to obtain multiple products, such as electricity, gasoline and diesel. To this end, this thesis investigates the feasibility of the operation and control of a novel cooling system which incorporates steam methane reformer (SMR) tubes into a gasifier radiant syngas cooler (RSC). This approach capitalizes on available exergy by producing valuable H<sub>2</sub>-rich synthesis gas (syngas) for liquid fuel production. As the device is still in the conceptual phase, a detailed multi-scale, two-dimensional, heterogeneous model has been developed in prior work to accurately predict the unit’s operation.</p> <p>A base case design was developed for both counter-current and co-current flow configurations, wherein a PI control structure designed to achieve performance objectives. Key trade-offs were found between the configurations: the counter-current design was more robust and effective in rejecting moderate and severe disturbances, while providing greater cooling duty and natural gas throughput, but at the expense of dangerously high tube wall temperatures, which can greatly reduce tube lifetime. The co-current design operates in a safer temperature range and satisfactorily rejects moderate disturbances, but requires feedforward control to handle extreme gasifier upsets.</p> <p>An offset-free linear model predictive controller (MPC) was developed for the co-current system to address process interactions. The MPC model was identified from ‘data’ derived from the rigorous plant model, with a Luenberger observer used to estimate and eliminate the plant-model mismatch. MPC offered superior set point tracking relative to discrete-PI control, especially in cases where discrete-PI destabilized the system. Using the co-current design, the flexibility of the device to adjust natural gas throughput based on variations in downstream syngas demand was demonstrated.</p> / Master of Applied Science (MASc)

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