Micro-inverse device capable of switching evaluation of catalyst and carbon determination of catalyst
A catalyst and reactor technology, applied in the field of micro-reactor devices, can solve the problems of combining reaction and carbon fixation, increasing experimental steps, etc., and achieve the effect of simple operation
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Embodiment 1
[0039] Baseline measurements were made using carbon black combustion.
[0040] (a) When the catalyst evaluation and carbon determination are not carried out, open the pressure stabilizing valve (1) and the mass flow meter (2), the electric six-way valve I (3) switches to the nitrogen gas path and enters the reactor, and the three-way valve ( 4) Switch to the nitrogen gas path. After the high-purity nitrogen gas passes through the mass flow meter (2) to control the flow rate, it enters the reactor for purge, and is directly emptied after passing through the electric six-way valve II (6) and the liquid separation tank (7). (b) Carbon black reference measurement: A certain amount of carbon black is charged into the reaction furnace (5) and sealed. Purging the gas path with nitrogen according to step (a), the temperature controller (26) raises the reaction furnace (5) to the carbon burning temperature. (c) Open the second pressure stabilizing valve (14) and the second mass flow m...
Embodiment 2
[0043] In the device of the present invention, the catalyst evaluation experiment and the catalyst carbon fixation reaction are switched.
[0044] (e) Catalyst evaluation reaction: A certain amount of catalyst is loaded into the reaction furnace (5) and sealed. Open the stop valve (12), the raw material pump (13), and switch the three-way valve (4) to the raw material pipeline. The raw material is fed through a micro raw material pump, and is gasified in the pipeline before the catalyst is installed in the micro reactor, and the reaction temperature of the reactor is set and controlled by a temperature controller. (f) After the raw materials are reacted in the reactor, they are directly emptied after passing through the electric six-way valve II (6) and the separatory tank (7). The electric six-way valve II (6) is in the incubator to ensure the gaseous state of the product. By changing the bubbling and detection state, the reaction product gas is cut into the chromatographic ...
Embodiment 3
[0047] On the device of the present invention, the modified silicon-aluminum-phosphorus molecular sieve is used as a catalyst, the loading amount of the catalyst is 3g, the loading amount of quartz sand is 3g, the pure raw material is injected, the partial pressure is 101Kpa, and the space velocity=10h -1 , the temperature of the reactor is 300°C. When the ratio of alcohol to agent was 1, the conversion rate of raw material was 100%, and the selectivity of product was 89.4%. When the ratio of alcohol to agent was 2.5, the conversion rate of raw material was 82%, and the selectivity of product was 92.3%. Catalyst carbon burning was carried out by electric three-way conversion, and the carbon dioxide peak area was 1101237773.4. According to the standard curve of carbon black burning carbon, the mass of coke attached to the catalyst was calculated to be 0.11125g, and the coke content of the catalyst was 375%.
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