Catalyst for double bond isomerization of butene
A double bond isomerization and catalyst technology, applied in physical/chemical process catalysts, isomerization hydrocarbon production, molecular sieve catalysts, etc., can solve the problems of low reaction product selectivity and short catalyst activity period.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0023] Refer to the preparation method of CN200310108177.5 to obtain silicon-aluminum molar ratio SiO 2 / Al 2 o 3 300 ZSM-5 molecular sieve.
[0024] Add 50 grams of the above-mentioned molecular sieves into 80 milliliters of an aqueous solution containing 2.0 grams of MgO, heat to dryness under stirring, then dry at 110° C. for 8 hours, roast at 580° C. for 2 hours, and pulverize. Add 8 grams of safflower essence and mix evenly, then add 20 grams of 40% by weight silica sol to adjust to a paste, and then extrude it into a bar shape of Φ2 mm by an extruder. After baking at 120 DEG C for 8 hours, then roasting at 550 DEG C for 4 hours, a catalyst containing 3% of MgO and 83% of molecular sieves was obtained in terms of weight percentage.
[0025] When the reaction temperature is 300°C, the reaction pressure is 0.5MPa, and the weight space velocity is 10 hours -1 Under the condition of certain conditions, the double bond isomerization reaction is carried out using refinery r...
Embodiment 2~15
[0027] Same preparation process as embodiment 1, change the SiO of molecular sieve 2 / Al 2 o 3 Molar ratio and rare earth content, get catalyst, and adopt refinery raffinate II to be raw material (by weight percentage, n-butane 16.8%, cis-2-butene 23.2%, trans-2-butene 60%), in Reaction temperature 310°C, reaction space velocity 6 hours -1 , under the condition that the reaction pressure is 0.5MPa, the reaction results are shown in Table 1 below.
[0028] Table 1
[0029]
[0030] Note: the alkaline earth content in the above examples is calculated based on the oxide content.
Embodiment 16
[0032] Adopt the catalyzer of embodiment 5, take refinery raffinate II as raw material (by weight percent, n-butane 16.8%, cis-2-butene 23.2%, trans-2-butene 60%), at reaction temperature 310 ℃, reaction space velocity 5 hours -1 , the reaction pressure is to carry out the catalyst stability (activity period) test under the condition of 0.8MPa, and its reaction result is as follows table 2:
[0033] Table 2
[0034]
[0035] The catalyst was tested for stability for 3300 hours, and the activity remained stable.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 