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Process for the decomposition of methyl tertiary-butyl ether

机译:甲基叔丁基醚的分解方法

摘要

Preparing isobutene, involves: (A) fractional distillation of methyl tert-butyl ether (MTBE)-containing stream comprising feed MTBE (I) and recycle stream (VIII) to give MTBE-containing overhead stream (II); (B) catalytic dissociation of stream (II) to give dissociation product (IV); (C) distillation of product (IV) into overhead stream (V) comprising isobutene (more than 90 mass.%) and bottom stream (VI); (D) fractional distillation of bottom stream (VI) to obtain methanol and MTBE (more than 99%) as overhead product (VIII); and (E) recirculation of product (VIII) to step (A). Preparing isobutene by dissociation of methyl tert-butyl ether (MTBE) in the gas phase, involves: (A) fractional distillation of an MTBE-containing stream comprising feed MTBE (I) and a recycle stream (VIII) to give an MTBE-containing overhead stream (II) and a bottom stream (III) having a boiling point higher than MTBE; (B) catalytic dissociation of the overhead stream (II) obtained in step (A) to give a dissociation product (IV); (C) separation by distillation of the dissociation product (IV) obtained in step (B) into an overhead stream (V) comprising isobutene (more than 90 mass.%) and a bottom stream (VI) comprising diisobutene, MTBE and more than 50% of the methanol present in the dissociation product (IV); (D) fractional distillation of the bottom stream obtained in step (C) under conditions under which the methanol is obtained as bottom product (VII) and MTBE (more than 99%) is obtained in the overhead product (VIII); and (E) recirculation of the overhead product (VIII) to step (A).
机译:异丁烯的制备涉及:(A)分馏包含进料MTBE(I)的含甲基叔丁基醚(MTBE)的料流和再循环料流(VIII),得到含MTBE的塔顶料流(II); (B)使物流(II)催化离解,得到离解产物(IV); (C)将产物(IV)蒸馏成包含异丁烯(大于90质量%)和塔底物流(VI)的塔顶物流(V); (D)对塔底料流(Ⅵ)进行分馏,得到甲醇和MTBE(99%以上),为塔顶产物(VIII); (E)将产物(VIII)再循环至步骤(A)。通过在气相中解离甲基叔丁基醚(MTBE)制备异丁烯,涉及:(A)分馏包含进料MTBE(I)的含MTBE料流和再循环料流(VIII),得到含MTBE的料沸点高于MTBE的塔顶料流(II)和塔底料流(III); (B)将步骤(A)中获得的塔顶料流(II)进行催化离解,得到离解产物(IV); (C)通过蒸馏将步骤(B)中获得的离解产物(IV)蒸馏分离成包含异丁烯(大于90质量%)的塔顶料流(V)和包含二异丁烯,MTBE和大于1%的塔底料流(VI)离解产物(IV)中存在的甲醇的50%; (D)在步骤(C)中得到的塔底物流在甲醇作为塔底产物(VII)得到和塔顶产物(VIII)中得到MTBE(大于99%)的条件下分馏; (E)将塔顶产物(VIII)再循环至步骤(A)。

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