Method for preparing polymer-grade isobutene by cracking methyl tertbutyl ether
A technology of methyl tert-butyl ether and isobutylene, which is applied in the field of methyl tert-butyl ether cracking to produce polymer-grade isobutylene, can solve the problems of difficult control of operating conditions, increased investment and operating costs of water washing towers, etc., and achieves convenient and flexible operation, The effect of high utilization rate and high purity
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preparation example Construction
[0025] figure 1 It is a typical schematic diagram of the preparation of high-purity isobutene. After MTBE is first refined through MTBE refining tower 1, it enters cracking reactor 2 to carry out cracking reaction under suitable operating conditions. The cracked product enters water washing tower 3, and the bottoms of water washing tower enter methanol recovery tower 4 and methanol refining tower 5 in turn. Methanol is recovered, and the crude isobutene product from the overhead of the water washing tower enters the isobutene de-weighting tower 6 and the isobutene de-lightening tower 7 in sequence, and finally the target product is obtained.
[0026] figure 2 It is a schematic diagram of the process for preparing high-purity isobutene of the present invention. After MTBE is first refined through MTBE refining tower 1, it enters cracking reactor 2 to carry out cracking reaction under suitable operating conditions. The cracked product enters water washing tower 3, and the bo...
Embodiment 1
[0043] An adsorption tower with a size of Φ100mm (inside)×1100mm is used, and the 13X molecular sieve, amorphous silica-alumina and 5A molecular sieve adsorbents used in comparative example 1, comparative example 3 and comparative example 5 with a size of 1.5mm are filled sequentially from bottom to top. 1 / 3 by volume. Raise the temperature of the adsorption tower to 80°C, and the volumetric space velocity is 500h -1 The crude product of isobutene, which has been kept at a constant temperature of 80°C, is metered from top to bottom at 0.1 MPa. Sampling and analysis every 4h. The results are shown in Table 4.
Embodiment 2
[0045] Use an adsorption tower with a size of Φ100mm (inner)×1100mm, and fill it with 1.5mm-sized 13X molecular sieves such as those used in Comparative Example 1, Comparative Example 3 and Comparative Example 5 from bottom to top at a volume ratio of 10:20:70. Shaped silica alumina and 5A molecular sieve. Raise the temperature of the adsorption tower to 80°C, and the volumetric space velocity is 500h -1 The crude product of isobutene, which has been kept at a constant temperature of 80°C, is metered from top to bottom at 0.1 MPa. Sampling and analysis every 4h. The results are shown in Table 4.
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