21 |
Biosorption by industrial microbial biomassMay, Harriet A. January 1984 (has links)
No description available.
|
22 |
Breaching the platinum cost curve: cost curve selection and development, marginal production survivalSchmitz, Peter January 2019 (has links)
A research report submitted in partial fulfilment of the requirements for the degree of Masters of Science in Engineering to the Faculty of Engineering and the Built
Environment, University of the Witwatersrand, Johannesburg, 2019 / The report considers survival mechanisms used by Platinum Group Metal
(PGM) producers over the period 2008 to 2017 when mining operations
were considered marginal for an extended period. Various methods to
build cost curves for the PGM industry were tested, with co-product
costing, inclusive of sustaining capital, selected. Industry cost curves
were developed for the period, showing that a significant portion of
producers were marginal from 2014 to 2017, with Impala lease area,
Rustenburg mines and Lonmin marginal for more than two years in that
period. Survival was achieved through cross-subsidisation, utilising cash
reserves, deferring sustaining capital, re-capitalisation and working capital
management, before ultimately restructuring through sale or closure took
place. While industry cost curves were effective at indicating operational
competitiveness in a particular year, a mechanism to indicate relative
financial strength (ability to sustain this position) needs to be sought. / TL (2020)
|
23 |
Vacuum refining of copperOzberk, Engin. January 1980 (has links)
No description available.
|
24 |
Evolução do refino de petróleo no Brasil / Evolution of petroleum refining in BrazilJuarez Barbosa Perisse 17 August 2007 (has links)
Este trabalho tem por objetivo apresentar a evolução da indústria do refino de petróleo no Brasil desde suas origens, sua evolução ao longo dos anos, explicitando as mudanças no perfil de produção, na matéria prima processada e na complexidade das nossas refinarias. Busca, também, apresentar os próximos passos para o refino de petróleo nacional, seus desafios face a produção de petróleos pesados e ácidos, bem como os impactos provocados pela necessidade de produção de derivados com especificações cada vez mais restritivas e com menor impacto ambiental. Optou-se pelo hidrorrefino como o primeiro grande passo para os próximos anos concluindo-se que unidades para o hidrotratamento de correntes intermediárias ou mesmo produto final assumirão um papel fundamental nos futuros esquemas de refino. Outra vertente importante analisada foi a necessidade de aumento de conversão, ressaltando-se que o caminho hoje escolhido de implantação de Unidades de Coqueamento Retardado se esgota no início da próxima década abrindo caminho para a tecnologia de hidroconversão de resíduo. Com relação à qualidade da gasolina e do óleo diesel foi apresentada uma proposta de esquema de refino para permitir o atendimento de especificações mais rígidas / This thesis aims to present the oil refining industry in Brazil since its origin, its evolution along the years, showing the changes in the production profile, in the crude oils processed and in the complexity of our refineries. Tries, additionally, to present the next steps for the national oil refining industry, its challenges facing the acid and heavy crude oil production, besides the impacts coming from the necessity of producing derivatives with stricter specifications and reduced environmental impact. Hydro-refining is showed to be the option for the next years, once intermediary and final products hydro-treating will assume a fundamental role on future refining scheme. Another important issue analyzed was the increased conversion necessity, highlighting that the current solution adopted which is the delayed coking units reaches its deadline in the beginning of the next decade, opening the door for residuum hydro-conversion technology. Related to gasoline and diesel oil quality, a refining configuration proposal was presented in order to achieve tighter specifications
|
25 |
Evolução do refino de petróleo no Brasil / Evolution of petroleum refining in BrazilJuarez Barbosa Perisse 17 August 2007 (has links)
Este trabalho tem por objetivo apresentar a evolução da indústria do refino de petróleo no Brasil desde suas origens, sua evolução ao longo dos anos, explicitando as mudanças no perfil de produção, na matéria prima processada e na complexidade das nossas refinarias. Busca, também, apresentar os próximos passos para o refino de petróleo nacional, seus desafios face a produção de petróleos pesados e ácidos, bem como os impactos provocados pela necessidade de produção de derivados com especificações cada vez mais restritivas e com menor impacto ambiental. Optou-se pelo hidrorrefino como o primeiro grande passo para os próximos anos concluindo-se que unidades para o hidrotratamento de correntes intermediárias ou mesmo produto final assumirão um papel fundamental nos futuros esquemas de refino. Outra vertente importante analisada foi a necessidade de aumento de conversão, ressaltando-se que o caminho hoje escolhido de implantação de Unidades de Coqueamento Retardado se esgota no início da próxima década abrindo caminho para a tecnologia de hidroconversão de resíduo. Com relação à qualidade da gasolina e do óleo diesel foi apresentada uma proposta de esquema de refino para permitir o atendimento de especificações mais rígidas / This thesis aims to present the oil refining industry in Brazil since its origin, its evolution along the years, showing the changes in the production profile, in the crude oils processed and in the complexity of our refineries. Tries, additionally, to present the next steps for the national oil refining industry, its challenges facing the acid and heavy crude oil production, besides the impacts coming from the necessity of producing derivatives with stricter specifications and reduced environmental impact. Hydro-refining is showed to be the option for the next years, once intermediary and final products hydro-treating will assume a fundamental role on future refining scheme. Another important issue analyzed was the increased conversion necessity, highlighting that the current solution adopted which is the delayed coking units reaches its deadline in the beginning of the next decade, opening the door for residuum hydro-conversion technology. Related to gasoline and diesel oil quality, a refining configuration proposal was presented in order to achieve tighter specifications
|
26 |
Incorporation of coloured impurities in sucrose crystalsGrimsey, I. M. January 1989 (has links)
No description available.
|
27 |
On Aspects Relating To A Hydrochlorination Facility For The Processing Of Refinery Precious Metal Residue Materials.Fortmann, Noel Alwin. January 1990 (has links)
A project report submitted to the Faculty of Engineering,
University of the Witwatersrand, Johannesburg in partial
fulfilment of the requirements for the Degree of Master
of Science in Engineering. / A hydrochlorination facility was developed for tile
processing of refinery precious metal residue materials
on the laboratory and pilot scale. Hazard
elements were identified and evaluated using an Event
Tree Analysis. An exponential technique was applied
to estimate the cost of the proposed production hydrochlorination
facility. The estimated cost was R120 000.
The Expected Present Value Ratio was +190 which indicated
satisfactory project economics.
The reactor material for the pilot scale unit was
selected using a weighted values quantitative material
selection procedure. Stainless steel Type 316L and
Type 310 were selected. Failure of the Type 516L
reactor occurred after 40 hours service. The mode of
failure was extensive surface scaling which was attributed
to the hydrogen chloride, sulphide gases and
1 000 °c operating envirornment.
Subject to certain provisions it would be feasible to
commission a safe and profitable production hydrochlorination
facility. The consumable reactor concept was
based on its replacement after 40 hours service. This
was justifiable because of the high value of the material
and the saving in down-stream processing costs. / Andrew Chakane 2018
|
28 |
Mechanical treatment of pulp fibers for property developmentHartman, Richard R. 01 January 1984 (has links)
No description available.
|
29 |
Heavy oil processing in steam and hydrogen plasmasKubanek, Gordon J. January 1985 (has links)
No description available.
|
30 |
The effect of rapid expansion conditions on the morphology of a model wax (n-octacosane)Griscik, Gregory J. 12 1900 (has links)
No description available.
|
Page generated in 0.0968 seconds