Phosphor and silicon-containing alumina supporter and preparing method thereof
A kind of technology of alumina support and alumina, which is applied in the direction of catalyst support, chemical instruments and methods, chemical/physical processes, etc., and can solve the problems affecting the surface properties and service performance of silicon-containing alumina support, and the inhomogeneity of alumina physical and chemical properties, etc. problem, to achieve the effect of improving catalyst level, easy molding, and high carrier strength
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preparation example Construction
[0013] The preparation process of phosphorus-containing, silicon-alumina carrier of the present invention is:
[0014] (1) The aluminum-containing salt solution is mixed with a precipitating agent under stirring conditions to obtain aluminum hydroxide precipitation, which is then aged, washed and filtered. Aluminum-containing salt solution and precipitation agent can be aluminum chloride and ammoniacal liquor, aluminum sulfate and ammoniacal liquor, aluminum nitrate and ammoniacal liquor, aluminum sulfate and sodium metaaluminate, sodium metaaluminate and nitric acid, sodium metaaluminate and carbon dioxide etc., preferably without Production of aluminum sulfate and sodium metaaluminate polluted by ammonia nitrogen. Conditions such as precipitation and aging can be properly adjusted according to the desired properties of alumina.
[0015] (2) beat the filter cake obtained by the above filtration, add phosphorus-containing compound, control the temperature of the slurry to 30-...
Embodiment 1
[0032] Step 1 Add 1200ml of deionized water to a clean container, heat up to 65°C, add sodium metaaluminate aqueous solution with a specific gravity of 1.35 at a flow rate of 30ml / min and aluminum sulfate aqueous solution with a specific gravity of 1.15 at a flow rate of 65ml / min, and simultaneously add Into stirred deionized water, maintain temperature 65°C, pH 8.5, add time 90 minutes.
[0033] Step 2 After stopping feeding, the system was aged for 90 minutes under the above pH and temperature conditions, and the filtered filter cake was slurried with deionized water, and washed with sodium carbonate solution for 5 times until Na + Content4 =Content+++ content <0.08m%.
[0034] Step 3 Add the aluminum hydroxide filter cake to a solution of 2.5L deionized water and 42g of 85m% phosphoric acid to make a slurry evenly, control the temperature of the slurry to 65°C, and filter after slurrying for 40 minutes.
[0035] In step 4, the filter cake was directly dried at 120° C. for ...
Embodiment 2
[0038] Step 1 is the same as Step 1 and Step 2 of Example 1.
[0039] Step 2 changes the 42.0g85m% phosphoric acid in embodiment 1 step 3 into 56g85m% phosphoric acid according to embodiment 2, i.e. the cost example, and the properties are shown in Table 1 (2).
[0040] Step 3 is the same as Step 4 and Step 5 of Embodiment 1.
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