Preparation method for wax temperature-sensitive medium for temperature control valve
A technology of temperature control valve and wax, which is applied in the field of preparation of temperature-sensing medium for wax-based heating temperature control valve, can solve the problems of unsuitable preparation of waxy temperature-sensing medium for temperature control valve, and achieve long service life and good use Effect, the effect of stable product performance
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Embodiment 1
[0025] (1) Hydrogenation of low-temperature F-T synthesis products:
[0026] The cold trap material in the F-T synthesis product (the F-T synthesis product is based on the catalyst in Example 1 of CN200910011993.1 and the cold trap material of the F-T synthesis product under corresponding conditions (that is, the fraction below 320 ° C) is the raw material of this example), in FHJ-2 Catalyst loaded with 0.8% K (FHJ-2 catalyst a Ni / Al2 o 3 Commercial catalyst, developed and produced by Fushun Petrochemical Research Institute, the content of active metal nickel is 40% in terms of oxides, impregnated with potassium nitrate and then dried and roasted) for hydrogenation under the conditions of 5MPa, 200°C, 2.0 LHSV and hydrogen-to-oil ratio 800 Conversion to convert olefins and oxygenates therein.
[0027] (2) Sweat the hydrogenation product obtained above:
[0028] Add the above-mentioned hydrogenation product (at a temperature of 35°C) into a traditional tank-type sweater, cool...
Embodiment 2
[0035] (1) Hydrogenation of low-temperature F-T synthesis products:
[0036] F-T synthesis product (F-T synthesis product is according to CN200910011987.6 Example 1 catalyst and synthetic light oil (that is, fraction below 350°C) in the F-T synthesis process under corresponding conditions is the raw material of this example), loaded on FV-10 catalyst with 1% K (FV-10 catalyst a W-Mo-Ni / Al 2 o 3 Type commercial catalyst, developed and produced by Fushun Petrochemical Research Institute, impregnated with potassium nitrate and then dried and roasted) under the action of 6MPa, 280°C, 2.0 LHSV and hydrogen-to-oil ratio of 300 for hydrogenation conversion to convert olefins and oxygenates therein.
[0037] (2) Sweat the hydrogenation product obtained above:
[0038] Add the above-mentioned hydrogenated product (at a temperature of 35°C) into a traditional tank-type sweater, cool down to 4°C at a rate of 1°C / h, then raise the temperature to 6°C at a rate of 1°C / h, and keep the temp...
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