Brand new animated movie, Khun Tong Dang the fresh new Motivations (dos015), is actually purposefully made for training girls and boys getting a positive personal feature. The modern research used that it motion picture because the example. The aim would be to understand the relationship between the a feature away from flick viewers as well as their impact of one’s a great feature away from a movie profile. One-hundred people off individuals age ranges taken care of immediately decimal forms. The questions incorporated what their age is, intercourse, impact regarding their personal characteristics, impact about their knowledge with folks, and you will impact concerning bravery, intelligence, and you will gratefulness of character. It actually was found that a beneficial private attribute have an effective experience of brand new impact regarding courage, cleverness, and you will gratefulness of reputation.

۲۷ A synopsis towards Abilities away from Brand name Mascot and you may Star Approval

Superstar and you will brand mascot affirmation were explored for more than thirty years. One another endorsers normally effectively import its profile to corporate photo and you will normally dictate clients purchasing this product. not, discover hidden concerning the mediators within number of approval and its own influence on purchasing conclusion. The intention of the current investigation should be to pick the brand new gab of your earlier in the day training and also to search you’ll mediators. It was found that consumers memories and you will identification certainly are the mediators, out-of supply dependability and you will acceptance feeling. A future investigation is prove the fresh model of affirmation, that has been created in the modern investigation.

twenty-six H2 Permeation Services regarding good Catalytic Membrane Reactor from inside the Methane Steam 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 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 sugar baby application Indianapolis IN 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 CH_cuatro 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.