Technical Officer. 3.6.1. To work with the individual, caseworker and occupational therapist to design suitable adaptations to the home;
Technical Officer. It was agreed that this expanded role would include: • Support teaching generally and provide “demonstrating” and/or “instruction” as necessary. • Assist in the design and development of practical classes. • Assist in the development/training of Demonstrators, subject to experience. • Assist in the development of student practical notebooks. • Commitment to continuing Professional Development, including taking on responsibilities consequent on new technologies. • Expanded role in research, which would involve supporting research activities, or a more inclusive role in Research Programmes and greater engagement in this area. This may involve additional training, for example with particular equipment and/or techniques. • Increased role for general administrative responsibilities, for example Health and Safety requirements, Stores and the assistance in activities such as budget control and purchasing etc. Technical staff at all grades may be redeployed along the lines of current agreements in each institution and/or as per attached appendices to this report.
Technical Officer. All work levels are performed in a Biomedical engineering or Medical Physics environment and are concerned with the management or repair/ calibration and clinical use of hospital based technology.
Technical Officer. Refining of petroleum feed stocks is an important process to produce environment-friendly liquid fuels and oils. Feed stocks today are becoming heavier and contain more sulphur; at the same time environmental regulations are becoming more stringent. To meet these challenges, highly efficient catalysts are required. Generally Mo, W metals supported on alumina and promoted by Co, Ni are used as hydrotreating catalysts. Catalytic efficiency of these catalysts can be enhanced by using supports with better physico-chemical properties than conventional γ-alumina. I n t h e p r e s e n t s t u d y v a r i o u s combinations of ZrO2-Al2O3 and MgO- Al2O3 mixed oxides were prepared by urea hydrolysis method as support for hydrotreating catalysts. Mo and W catalysts promoted by Co and Ni were prepared on selected supports by incipient wetness method. All the s u p p o r t s a n d c a t a l y s t s w e r e has Bronsted acidity. Total acidity i n c r e a s e s p r o p o r t i o n a l l y o n incorporation of ZrO2 into the matrix of Al2O3. MgO is basic in nature; its mixed oxides with alumina showed a decrease in total acidity with an increase in MgO content. It seems to follow the simple acid-base neutralization mechanism. Generation of acidity in mixed oxides on variation of composition starts from weak to strong acid sites whereas neutralization takes place from strong to weak acid sites. Strong acid sites present in ZrO2-Al2O3 mixed oxides and total acidity of MgO-Al2O3 mixed oxides are in good agreement with cumene cracking activity. Surface area data and activity results showed that 8 wt % Mo is sufficient to form the monolayer of MoO3 on both the mixed oxides surfaces. TPR results showed that the ratio of hydrogen consumption of the first peak to the second peak is 1:2, which indicates that Based on these studies, Mr Xxxxx Xxxxx, Te c h n i c a l O f f i c e r , published six research papers in the leading journals of catalysis area and submitted a thesis to the H N B Garhwal University, Srinagar (Garhwal), from where he was awarded Ph D Degree in January 2007. The Ph D work was supervised by Dr X Xxxxxx Xxxx, Senior Scientist, IIP. vacancies which are responsible for oxygen uptake are also an active centre for HDS, HYD and HYC catalytic functionalities. Co (3 wt %) was found to be the optimum amount to promote 8 wt % Mo support on both the mixed oxides. Results showed that 19 wt % W is sufficient to form the monolayer of WO3 on the surfaces of both the mixed oxi...
