Method for measuring wear rate of catalyst
A measurement method and wear rate technology, which can be used in the preparation of test samples, weighing by removing certain components, and chemical analysis by combustion. Highly maneuverable and repeatable effects
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Embodiment 1
[0043] This embodiment is used to illustrate the test method of catalyst wear performance provided by the present invention
[0044] (1) 10g of iron-based Fischer-Tropsch synthesis catalyst A and 600ml of liquid paraffin are filled in a 1L stirred tank reactor, and the diameter of the stirring paddle is about 5cm. h 2 and CO, the catalyst is first heated at 250°C with a space velocity of 5000h -1 , the ratio of hydrogen to carbon is 5.0, and the stirring speed is adjusted so that the tangential line speed is 1m / s and the reduction is 24h. Switch to 250°C after catalyst reduction, 2.3MPa, space velocity 8000h -1 , the hydrogen-to-carbon ratio is 3.0, and the stirring speed is adjusted so that the tangential line speed is 8m / s and the reaction is maintained for 200h.
[0045] (2) After the reaction is over, cool down to 130°C and reduce the pressure to normal pressure. After the stirring is stopped, quickly put the stirred tank body filled with the slurry in the still in an o...
Embodiment 2
[0048] This embodiment is used to illustrate the test method of catalyst wear performance provided by the present invention
[0049] The catalyst abrasion performance test was carried out according to the method of Example 1, except that the iron-based Fischer-Tropsch synthesis catalyst A was replaced by an equivalent amount of iron-based Fischer-Tropsch synthesis catalyst B.
[0050] The iron content in the sample was analyzed by inductively coupled plasma spectrometer (ICP), the results are shown in Table 1, and the experiment was repeated 3 times.
Embodiment 3
[0052] This embodiment is used to illustrate the test method of catalyst wear performance provided by the present invention
[0053] (1) 10g of iron-based Fischer-Tropsch synthesis catalyst C and 800ml of liquid paraffin are filled in a 1L stirred tank reactor, and the diameter of the stirring paddle is about 5cm. h 2 and CO, the catalyst is first heated at 250°C with a space velocity of 5000h -1 , the ratio of hydrogen to carbon is 5.0, and the stirring speed is adjusted so that the tangential line speed is 1m / s and the reduction is 24h. Switch to 280°C after catalyst reduction, 2MPa, space velocity 15000h -1 , the hydrogen-to-carbon ratio is 2.5, and the stirring speed is adjusted so that the tangential line speed is 10m / s and the reaction is maintained for 100h.
[0054] (2) After the reaction, cool down to 150°C, reduce the pressure to normal pressure, stop the stirring, and quickly place the stirred tank body containing the slurry in the kettle in an oven at 150°C for ...
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