The fresh animated film, Khun Tong Dang this new Motivations (2015), is actually purposefully made for teaching young ones to own an optimistic private characteristic. The current investigation utilized it film as example. The aim is to comprehend the dating between your a great trait of film audiences in addition to their impression of the an effective trait regarding a film profile. One-hundred youngsters from individuals age brackets responded to decimal questionnaires. The questions included their age, gender, impression about their personal attributes, perception about their experiences with folks, and you will impression concerning bravery, cleverness, and you will gratefulness of reputation. It was found that a great individual trait features a strong experience of the fresh new effect away from courage, intelligence, and you can gratefulness of one’s profile.
27 A synopsis to your Functionality off Brand name Mascot and Superstar Approval
Star and you may brand mascot acceptance was indeed searched for more than three decades. One another endorsers can effortlessly transfer their profile so you’re able to business visualize and you will can also be influence the clients to acquire the product. not, there clearly was hidden towards mediators within level of endorsement as well as effect on to acquire choices. The intention of the current investigation is always to choose the fresh gab of your own past knowledge and also to look for you can easily mediators. It actually was unearthed that consumers memory and identification could be the mediators, out-of supply dependability and you will acceptance effect. A future research should confirm brand new make of acceptance, that was established in the modern investigation.
26 H2 Permeation Services out-of a beneficial Catalytic Membrane layer Reactor inside Methane Steam 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 https://cdn.datingnode.com/file/scale/_98264__2680174/_800x800__1521046950.jpg” alt=”Minneapolis MN sugar daddy”> 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.
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