The brand new mobile movie, Khun Tong Dang new Motivations (dos015), is intentionally created for practise youngsters to own a positive private trait. The current research utilized so it film because the research study. The aim is to see the sugardaddy.com relationships amongst the good attribute from movie watchers as well as their perception of the a beneficial attribute out of a motion picture profile. One-hundred people out-of various age brackets responded to decimal surveys. The questions provided how old they are, sex, perception regarding their own personal characteristics, impression regarding their knowledge with people, and you may effect regarding the bravery, cleverness, and you will gratefulness of your own reputation. It had been learned that good private feature possess a robust experience of the perception away from bravery, cleverness, and you will gratefulness of your own character.
27 A summary for the Capability regarding Brand Mascot and Star Affirmation
Celebrity and you can brand name mascot approval was basically explored for more than thirty years. Both endorsers is also efficiently transfer their character so you can business visualize and you will is determine the shoppers to buy the merchandise. However, there clearly was hidden concerning mediators between the number of acceptance and its particular affect to find decisions. The intention of the present day data is always to choose the fresh gab of prior education and to look for you’ll mediators. It was learned that customers recollections and you can character could be the mediators, out-of origin dependability and you may approval feeling. Another data is always to prove the fresh brand of approval, that has been established in the current studies.
twenty-six H2 Permeation Functions from a beneficial Catalytic Membrane layer Reactor from inside the Methane Vapor Reforming Response
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 its higher surface area compared to the catalytic layer.