The newest animated motion picture, Khun Tong Dang the fresh Motivations (2015), is purposefully created for teaching children to have an optimistic private attribute. The current investigation utilized so it flick since the example. The goal would be to comprehend the relationship between the an excellent characteristic out of movie audience as well as their feeling of your good feature out-of a movie profile. One-hundred or so people regarding various age ranges responded to quantitative forms. The questions integrated their age, intercourse, impact regarding their own private attributes, impression regarding their enjoy with people, and impact in regards to the bravery, intelligence, and gratefulness of your reputation. It actually was discovered that a individual attribute possess a powerful experience of new perception regarding bravery, cleverness, and you will gratefulness of profile.
twenty-seven An overview towards Abilities off Brand Mascot and you may Celebrity Acceptance
Star and you can brand mascot approval was searched for over three decades. Each other endorsers normally efficiently import the character so you can business photo and is influence the customers to shop for the merchandise. not, discover little-known regarding mediators between your number of acceptance and its influence on to invest in behavior. The purpose of the present day studies should be to choose this new gab of one’s earlier degree also to look for you’ll be able to mediators. It was unearthed that consumers memory and you may identification would be the mediators, regarding origin credibility and you may acceptance effect. Another study is to show the make of endorsement, that has been created in the present day study.
twenty-six Halifax sugar baby H2 Permeation Services off a Catalytic Membrane layer Reactor in 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 its higher surface area compared to the catalytic layer.