Brand new move film, Khun Tong Dang the new Motivations (dos015), is purposefully designed for exercises offspring for a positive individual characteristic. The modern investigation used which movie as the case study. The target will be to comprehend the matchmaking between your a great characteristic regarding motion picture audience as well as their perception of good attribute off a motion picture character. One-hundred or so pupils off individuals age brackets responded to decimal questionnaires. All the questions integrated how old they are, sex, feeling about their own private attributes, perception regarding their experience with others, and perception concerning bravery, cleverness, and you may gratefulness of the reputation. It absolutely was discovered that a beneficial individual feature have a powerful experience of this new impression out of courage, cleverness, and gratefulness of your profile.
27 An overview towards the Functionality out of Brand Mascot and you may Superstar Endorsement
Celebrity and you may brand name mascot affirmation have been browsed for more than thirty years. One another endorsers can be effortlessly transfer the character in order to business picture and normally determine the shoppers buying this product. However, there was hidden concerning the mediators amongst the quantity of approval as well as influence on to get decisions. The intention of the current investigation will be to select the brand new gab of your earlier training and also to search possible mediators. It absolutely was found that users thoughts and identification certainly are the mediators, out of supply credibility and you may acceptance impression. The next analysis would be to confirm the fresh new brand of approval, that has been created in the current data.
26 H2 Permeation Services regarding an effective Catalytic Membrane Reactor within the Methane Vapor Reforming Effect
Cylindrical alumina microfiltration membrane (GMITM Corporation, inside diameter=9 mm, outside diameter=13 mm, length= 50 mm) with an average pore size of 0.5 micrometer and porosity of about 0.35 was used as the support for membrane reactor. This support was soaked in boehmite sols, and the mean particle size was adjusted in the range of 50 to 500 nm by carefully controlling hydrolysis time, and calcined Liverpool sugar babies at 650 °C for two hours. This process was repeated with different boehmite solutions in order to achieve an intermediate layer with an average pore size of about 50 nm. The resulting substrate was then coated with a thin and dense layer of silica by counter current chemical vapour deposition (CVD) method. A boehmite sol with 10 wt.% of nickel which was prepared by a standard procedure was used to make the catalytic layer. BET, SEM, and XRD analysis were used to characterize this layer. The catalytic membrane reactor was placed in an experimental setup to evaluate the permeation and hydrogen reforming reaction. The setup consisted of a tubular module in which the membrane was fixed, and the reforming reaction occurred at the inner side of the membrane. Methane stream, diluted with nitrogen, and deionized water with a steam to carbon (S/C) ratio of 3.0 entered the reactor after the reactor was heated up to 500 °C with a specified rate of 2 °C/ min and the catalytic layer was reduced at presence of hydrogen for 2.5 hours. Nitrogen flow was used as sweep gas through the outer side of the reactor. Any liquid produced was trapped and separated at reactor exit by a cold trap, and the produced gases were analyzed by an on-line gas chromatograph (Agilent 7890A) to measure total CHcuatro conversion and H2 permeation. BET analysis indicated uniform size distribution for catalyst with average pore size of 280 nm and average surface area of 275 m 2 .g -1 . Single-component permeation tests were carried out for hydrogen, methane, and carbon dioxide at temperature range of 500-800 °C, and the results showed almost the same permeance and hydrogen selectivity values for hydrogen as the composite membrane without catalytic layer. Performance of the catalytic membrane was evaluated by applying membranes as a membrane reactor for methane steam reforming reaction at gas hourly space velocity (GHSV) of 10,000 h ?1 and 2 bar. CH4 conversion increased from 50% to 85% with increasing reaction temperature from 600 °C to 750 °C, which is sufficiently above equilibrium curve at reaction conditions, but slightly lower than membrane reactor with packed nickel catalytic bed because of its higher surface area compared to the catalytic layer.