化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
3期
781-785
,共5页
岳金彩%孙可慧%程华农%郑世清
嶽金綵%孫可慧%程華農%鄭世清
악금채%손가혜%정화농%정세청
乙醇胺%热敏性%模拟%集成%分离
乙醇胺%熱敏性%模擬%集成%分離
을순알%열민성%모의%집성%분리
ethanolamine%heat sensitivity%simulation%integration%separation
乙醇胺生产中的氨水浓度对能耗有很大影响,需要对脱氨脱水工艺进行能量集成以降低能耗,同时乙醇胺又是热敏性物质,操作温度限制成为能量集成时要考虑的因素。本文实验研究了含水和不含水乙醇胺混合物的色号随温度、停留时间的变化规律,确定160℃为脱氨脱水工艺的操作温度上限。在不同氨水浓度下,对未进行能量集成的能耗和各塔操作条件进行了比较,结果表明当氨水浓度达到45%时,脱氨塔底温度为160.2℃,已大于操作温度上限,需要改变脱氨操作才能满足温度限制。通过提高脱水塔操作压力,使其塔顶蒸汽为脱氨塔和真空脱水塔提供能量,针对不同氨水浓度,对3种热量集成方案进行了研究。结果表明,由于受到操作温度限制,不同氨水浓度的脱氨脱水工艺需要采取不同的集成方案。
乙醇胺生產中的氨水濃度對能耗有很大影響,需要對脫氨脫水工藝進行能量集成以降低能耗,同時乙醇胺又是熱敏性物質,操作溫度限製成為能量集成時要攷慮的因素。本文實驗研究瞭含水和不含水乙醇胺混閤物的色號隨溫度、停留時間的變化規律,確定160℃為脫氨脫水工藝的操作溫度上限。在不同氨水濃度下,對未進行能量集成的能耗和各塔操作條件進行瞭比較,結果錶明噹氨水濃度達到45%時,脫氨塔底溫度為160.2℃,已大于操作溫度上限,需要改變脫氨操作纔能滿足溫度限製。通過提高脫水塔操作壓力,使其塔頂蒸汽為脫氨塔和真空脫水塔提供能量,針對不同氨水濃度,對3種熱量集成方案進行瞭研究。結果錶明,由于受到操作溫度限製,不同氨水濃度的脫氨脫水工藝需要採取不同的集成方案。
을순알생산중적안수농도대능모유흔대영향,수요대탈안탈수공예진행능량집성이강저능모,동시을순알우시열민성물질,조작온도한제성위능량집성시요고필적인소。본문실험연구료함수화불함수을순알혼합물적색호수온도、정류시간적변화규률,학정160℃위탈안탈수공예적조작온도상한。재불동안수농도하,대미진행능량집성적능모화각탑조작조건진행료비교,결과표명당안수농도체도45%시,탈안탑저온도위160.2℃,이대우조작온도상한,수요개변탈안조작재능만족온도한제。통과제고탈수탑조작압력,사기탑정증기위탈안탑화진공탈수탑제공능량,침대불동안수농도,대3충열량집성방안진행료연구。결과표명,유우수도조작온도한제,불동안수농도적탈안탈수공예수요채취불동적집성방안。
The ammonia content has a significant effect on consumption of energy in production of ethanolamine (EA). Heat integration is needed to reduce energy consumption in the process of ammonia and water removal. At the same time,operating temperature limitation should be considered because EA is a heat sensitive material. This paper studied variation of color numbers of the EA mixtures with or without water with the changing temperature and residence time. It was determined that 160 ℃ was the upper limit of operating temperature limitation in the process of ammonia and water removal. For different ammonia contents,the non-integrated energy consumptions and column operating conditions of process were compared. The results showed the temperature of de-ammonia column was 160.2 ℃ slightly over the temperature limitation. Therefore,the operation of ammonia removal would need to be adjusted. Three types of heat integration schemes were studied under different ammonia contents. The results showed that,the integration solutions of ammonia and water removal were different for different ammonia contents due to the operating temperature limitation.