本文采用异丁烯两步法生产甲基丙烯酸甲酯，该工艺分两个工段，首先完成甲基

本文采用异丁烯两步法生产甲基丙烯酸甲酯，该工艺分两个工段，首先完成甲基丙烯醛的合成。原料异丁烯以及辅助原料先后经过甲基丙烯醛合成反应器，异丁烯现在催化剂存在的条件下被氧化，过程中生成的气体经急冷喷淋塔，脱水塔和排气塔。排气塔塔顶为极少量未反应的异丁烯，氮气及氧气，还有很小一部分中间过程生成的气体杂质，都进入火炬系统处理。

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结果 (英语) 1: [复制]

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In this paper, the isobutylene two-step method is used to produce methyl methacrylate. The process is divided into two sections. First, the synthesis of methacrolein is completed. The raw material isobutene and auxiliary raw materials pass through the methacrolein synthesis reactor successively. The isobutene is now oxidized in the presence of the catalyst, and the gas generated in the process passes through the quench spray tower, dehydration tower and exhaust tower. The top of the exhaust tower contains a very small amount of unreacted isobutylene, nitrogen and oxygen, and a small part of the gas impurities generated in the intermediate process, all of which enter the flare system for processing.

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结果 (英语) 2:[复制]

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In this paper, the two-step method of isobutene production of methyl acrylic, the process is divided into two sections, the first complete the synthesis of methyl acrylic. Raw material isobutene and auxiliary raw materials have passed methyl acrylic synthesis reactor, isobutene is now the presence of catalyst conditions are oxidized, the process of the gas generated by the rapid cold spray tower, dewatering tower and exhaust tower. The top of the exhaust tower is a very small amount of unresponsive isobutene, nitrogen and oxygen, as well as a small fraction of the gas impurities generated by the intermediate process, all of which are processed into the torch system.

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结果 (英语) 3:[复制]

复制成功！

In this paper, methyl methacrylate is produced by isobutene two-step process. The process is divided into two stages. Firstly, the synthesis of methylacrolein is completed. The raw material isobutene and auxiliary raw material successively pass through the methacrolein synthesis reactor, isobutene is oxidized in the presence of catalyst, and the gas generated in the process passes through the quench spray tower, dehydration tower and exhaust tower. A very small amount of unreacted isobutene, nitrogen and oxygen at the top of the exhaust tower, as well as a small part of the gas impurities generated in the intermediate process, enter the flare system for treatment.<br>

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