Method of synthesizing silicon phosphorus aluminium molecular sieve
A silicon-phosphorus-aluminum molecular sieve and silicon source technology, applied in molecular sieve catalysts, molecular sieves and alkali-exchanged phosphates, molecular sieve characteristic silicon-aluminophosphates, etc., can solve the problems of low selectivity of low-carbon olefins, large molecular sieve grains, and high synthesis costs problem, to achieve the effect of improving catalytic performance, uniform particle size, and benefiting acid control
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Embodiment 1~2 and comparative example 1~2
[0018] Synthesis of SAPO-34 Molecular Sieve
[0019] According to the formula (x·TEAOH+y·Morpholine): 0.6SiO 2 :Al 2 o 3 :P 2 o 5 : 60H 2 O Weigh the raw material. The values of x and y are shown in Table 1.
[0020] Example
product number
TEAOH: Morpholine (mol)
XRD
Grain size (micron)
Comparative example 1
S-01
1.0∶0.0
SAPO-34
0.6
Example 1
S-02
0.2∶0.8
SAPO-34
1.8
Example 2
S-03
0.1∶0.9
SAPO-34
17
Comparative example 2
S-04
0∶1.0
SAPO-34
35
[0021] A certain amount of γ-Al 2 o 3 ·H 2 O and fully stir and mix with orthophosphoric acid aqueous solution to form a uniform jelly. Keep stirring, add silica sol, template agent morpholine and a small amount of tetraethylammonium hydroxide in sequence, and finally add a certain amount of deionized water. After fully stirring, a crystallization mixed liquid is formed. The cryst...
Embodiment 3
[0024] Preparation of SAPO-34 Molecular Sieve Catalyst
[0025] The original powders S-01, S-02, S-03 and S-04 prepared in Examples 1-2 and Comparative Examples 1-2 were sequentially roasted at 600°C for 3.0 hours to remove the template agent, and then tableted 1. After crushing, sieve the 30-mesh particle size, and obtain catalysts serially numbered CS-01, CS-02, CS-03 and CS-04, pending evaluation.
Embodiment 4
[0027] SAPO-34 molecular sieve catalyst
[0028] Using a fixed-bed catalytic reaction device, CS-01, CS-02, CS-03 and CS-04 obtained in Example 3 were respectively subjected to catalyst evaluation experiments. The experimental conditions are that the catalyst loading is 1.46 grams, the reaction temperature is 450°C, the reaction pressure is normal pressure, and the weight space velocity of methanol and water is 1.25 hours respectively. -1 and 3.75 hours -1 , the nitrogen flow rate is 50 ml / min. The results are shown in Table 2.
[0029] sample
Conversion rates
(weight%)
reaction
time *
(Hour)
Hydrocarbon product distribution (wt%)
CH 4
C 2 h 6
C 2 h 4
C 3 h 8
C 3 h 6
C 4 h 10
C 4 h 8
C 5 +
C 2 = ~C 4 =
CS-01
100%
6.0
1.74
0.35
54.24
0.56
33.09
0.089
8.21
2....
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