CN101423468A - 一种醋酸裂解的方法 - Google Patents

一种醋酸裂解的方法 Download PDF

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CN101423468A
CN101423468A CNA200710134644XA CN200710134644A CN101423468A CN 101423468 A CN101423468 A CN 101423468A CN A200710134644X A CNA200710134644X A CN A200710134644XA CN 200710134644 A CN200710134644 A CN 200710134644A CN 101423468 A CN101423468 A CN 101423468A
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acetic acid
cracking
vaporizer
acid cracking
fuel
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CN101423468B (zh
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刘纪才
包忠祥
沈德智
刘惠兴
陈小萍
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Nantong Hongxin Chemical Co ltd
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ZHANGJIAGANG HAOBO CHEMICAL PRODUCT CO Ltd
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Abstract

本发明公开了一种能使生产成本大大降低的醋酸裂解的方法,其特点是:在醋酸裂解过程中使用煤气作为燃料。本发明的优点是:1.醋酸裂解过程中采用易得、价廉的煤气作为燃料可大大节约生产成本;2.醋酸汽化过程不需配套外接蒸汽作为热源从而减少了外界因素对生产的干扰;3.将出裂解炉的烟气引入醋酸汽化器的加热管中,烟气的热量被进一步利用后排空。

Description

一种醋酸裂解的方法
技术领域
本发明涉及醋酸裂解的方法,具体涉及以醋酸为原料裂解制取乙烯酮、双乙烯酮等的方法。
背景技术
醋酸裂解是以醋酸为原料制取乙烯酮、双乙烯酮等产品的关键,在裂解过程中其加热方法及所取用的燃料或加热源是否科学等都将对其最终的产能、成本和质量带来举足轻重的影响。目前化工行业中的醋酸裂解方法为:首先将醋酸配制成92%左右的醋酸水溶液,然后将配制好的醋酸水溶液匀速加入醋酸汽化器内,目前使用盘管蒸汽来加热醋酸汽化器使醋酸水溶液汽化成醋酸蒸汽,汽化后的醋酸蒸汽进入预热炉,经预热后的醋酸蒸汽进入裂解炉炉管,裂解炉底部采用燃油喷枪加热裂解炉炉管,燃油产生的烟气由裂解炉进入预热炉后未加利用直接排空,醋酸蒸汽经裂解炉裂解后变成乙烯酮和水,然后被送入后段进行分离和冷却。上述裂解方法的不足有:1、采用燃油加热成本高,每生产一吨双乙烯酮需燃料成本约为1300元/吨;2、燃烧后的烟气排出温度达500℃以上,热量浪费大;3、醋酸汽化器需配套蒸汽供应装置,并且在裂解炉前还需单独配备预热炉,设备结构较复杂,投资也较大;4、近年来国际油价也是一涨再涨,由此给以醋酸为原料裂解生产乙烯酮、双乙烯酮等产品的企业带来空前的成本压力,。
发明内容
本发明所要解决的技术问题是:将提供一种能使生产成本大大降低的醋酸裂解方法。
为解决上述技术问题,本发明采用的技术方案是:所述的一种醋酸裂解的方法,其特点是:在醋酸裂解过程中使用煤气作为燃料。
本发明进一步的技术方案是:在醋酸裂解过程中,同时将裂解炉所产生的高温烟气引入到醋酸汽化器内,作为醋酸汽化器内加热管的热源。
本发明的优点是:1、醋酸裂解过程中采用易得、价廉的煤气作为燃料可大大节约生产成本;2、醋酸汽化过程不需配套外接蒸汽作为热源从而减少了外界因素对生产的干扰;3、将出裂解炉的烟气引入醋酸汽化器的加热管中,烟气的热量被进一步利用后排空;。
具体实施方式
下面通过具体实施例对本发明作进一步的描述,但本发明并不仅限于此实施例。
调整好煤气发生炉使煤气热值保持在1200Kcal/M3,将99.5%的醋酸加水配制成92%的醋酸水溶液,点燃裂解炉下部的煤气烧嘴,当炉体温度达700℃时,将92%的醋酸按500L/h的流量连续加入醋酸汽化器内,煤气燃烧产生的烟气加热裂解炉炉管后再流经汽化器使醋醋汽化器内的醋酸汽化,调节煤气的加入量维持裂解炉出口温度为700~710℃,此时汽化器内醋酸气体温度为120℃,此时测得出汽化器的烟气温度为145℃,连续生产48小时后得到以下数据:煤气发生炉耗煤12吨,获得双乙烯酮15吨,计算所得每吨双乙烯酮的燃料成本为1100元,比以油为燃料的生产方法下降了20%。并且醋酸汽化过程不需配套外接蒸汽作为热源从而减少了外界因素对生产的干扰;将出裂解炉的烟气引入醋酸汽化器的加热管中,烟气的热量被进一步利用后排空。

Claims (2)

1、一种醋酸裂解的方法,其特征在于:在醋酸裂解的过程中使用煤气作为燃料。
2、如权利要求1所述的醋酸裂解的方法,其特征在于:在醋酸裂解过程中,同时将裂解炉所产生的高温烟气引入到醋酸汽化器内,作为醋酸汽化器内加热管的热源。
CN200710134644A 2007-11-02 2007-11-02 一种醋酸裂解的方法 Active CN101423468B (zh)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110283060A (zh) * 2019-07-12 2019-09-27 抚顺顺特化工有限公司 一种3.3二甲基丙烯酸的合成工艺

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110283060A (zh) * 2019-07-12 2019-09-27 抚顺顺特化工有限公司 一种3.3二甲基丙烯酸的合成工艺

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