New transferring motion picture, Khun Tong Dang the Motivations (2015), was purposefully made for practise girls and boys getting an optimistic private feature. The present day study used so it flick while the case study. The target is always to see the matchmaking between your an effective attribute off movie viewers as well as their impact of your own a great feature out of a movie profile. One-hundred or so people regarding certain age ranges taken care of immediately quantitative surveys. The questions integrated what their age is, intercourse, effect about their own private qualities, effect about their enjoy with folks, and you may impression concerning the bravery, cleverness, and you may gratefulness of your profile. It was discovered that a good personal characteristic keeps a strong experience of the fresh new feeling out-of bravery, cleverness, and gratefulness of reputation.
twenty-seven A summary towards Features off Brand Mascot and you may Superstar Endorsement
Superstar and you can brand name mascot acceptance have been browsed for more than 3 decades. One another endorsers is effortlessly transfer their profile in order to business image and you can is dictate the customers to purchase the item. Although not, there’s little-known concerning mediators within number of approval and its own influence on to invest in conclusion. The goal of the current data is to select the fresh new gab of your past education and seek you are able to mediators. It absolutely was found that customers thoughts and you will identity would be the mediators, from resource dependability and you may acceptance feeling. A future research is establish the fresh make of approval, which was created in the present day research.
twenty-six H2 Permeation Functions out of an effective Catalytic Membrane Reactor during the Methane Vapor Reforming Impulse
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 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 sugar daddy site Edinburg TX its higher surface area compared to the catalytic layer.