スタッフブログ

It absolutely was crucial that you see the feeling out-of news in more youthful teenagers

2022.08.01

It absolutely was crucial that you see the <a href="https://sugardaddydates.net/sugar-daddies-canada/winnipeg/">Winnipeg sugar babies website</a> feeling out-of news in more youthful teenagers

This new animated film, Khun Tong Dang this new Inspirations (2015), are intentionally created for training children to have an optimistic private attribute. The present day research made use of that it flick since the case study. Objective will be to understand the dating amongst the a great attribute away from motion picture people in addition to their feeling of your own a good attribute out of a film character. One-hundred or so youngsters of various age brackets responded to decimal questionnaires. All the questions integrated what their age is, intercourse, effect regarding their own personal qualities, perception regarding their enjoy with others, and feeling towards bravery, intelligence, and you can gratefulness of your own reputation. It was found that an excellent personal characteristic possess a strong reference to this new impression from courage, intelligence, and you may gratefulness of your reputation.

27 A synopsis on the Functionality away from Brand Mascot and you can Superstar Endorsement

Celebrity and you may brand mascot approval was browsed for over thirty years. Both endorsers normally efficiently import the reputation so you’re able to corporate visualize and can determine the purchasers to order the product. Although not, discover little-known regarding mediators between the quantity of affirmation and its own affect to purchase conclusion. The objective of the modern investigation is always to select the newest gab of previous degree and find possible mediators. It actually was learned that consumers recollections and you may identity would be the mediators, out-of source trustworthiness and you will affirmation effect. A future research would be to show new model of acceptance, that was established in the current studies.

twenty six H2 Permeation Functions off good Catalytic Membrane Reactor inside Methane Steam 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.