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低溫余熱回收技術(shù)在芳烴聯(lián)合裝置中應(yīng)用

發(fā)布時(shí)間:2018-06-23 22:13

  本文選題:芳烴聯(lián)合裝置 + 低溫?zé)峄厥绽眉夹g(shù)。 參考:《華南理工大學(xué)》2014年碩士論文


【摘要】:本文論述了低溫余熱回收在當(dāng)今提倡綠色低碳社會(huì)的重要性,以及低溫余熱回收技術(shù)的應(yīng)用現(xiàn)狀。芳烴聯(lián)合裝置是煉化企業(yè)中典型的高耗能裝置,在海南煉化60萬(wàn)噸/年芳烴裝置投產(chǎn)以前,世界上所有的芳烴裝置均被美國(guó)UOP、法國(guó)IFP技術(shù)壟斷,這些裝置中大量的塔頂?shù)蜏責(zé)崃亢头磻?yīng)物料余熱均采用常規(guī)的空冷冷卻方式,不僅浪費(fèi)塔頂?shù)蜏赜酂,而且空冷風(fēng)機(jī)也同時(shí)消耗大量電能。中國(guó)石化海南煉油化工有限公司(簡(jiǎn)稱(chēng)海南煉化)芳烴聯(lián)合裝置采用中國(guó)石化自主知識(shí)產(chǎn)權(quán)的工藝包技術(shù),在節(jié)能降耗方面有很大突破,一方面對(duì)于傳統(tǒng)工藝中塔頂溫度稍高的塔,通過(guò)適當(dāng)提高塔頂壓力、溫度,使其能夠產(chǎn)生0.45MPa蒸汽,發(fā)出的蒸汽經(jīng)過(guò)加熱爐對(duì)流段過(guò)熱后,推動(dòng)汽輪機(jī)發(fā)電;另一方面對(duì)于塔頂溫度相對(duì)較低的塔,塔頂設(shè)置熱水換熱器,將熱水換熱至120℃后,送至卡琳娜循環(huán)熱水發(fā)電系統(tǒng)和ORC熱水發(fā)電系統(tǒng)發(fā)電。通過(guò)此項(xiàng)技術(shù)回收利用裝置內(nèi)絕大部分低溫?zé)崃。目前,,整個(gè)裝置的發(fā)電量已超過(guò)裝置的用電量,實(shí)現(xiàn)了芳烴聯(lián)合裝置不耗電,還向外輸出電的良好效果,并通過(guò)能耗對(duì)比進(jìn)一步驗(yàn)證了低溫余熱回收技術(shù)的先進(jìn)性。此項(xiàng)技術(shù)的成功應(yīng)用,對(duì)有大量低溫?zé)岽嬖诘臒捰突、冶金、鋼鐵、火電等行業(yè)進(jìn)行節(jié)能優(yōu)化具有重要的指導(dǎo)意義,且具有廣闊的應(yīng)用前景。
[Abstract]:This paper discusses the importance of low temperature waste heat recovery in green and low carbon society, and the application status of low temperature waste heat recovery technology. The aromatics combination unit is a typical high energy consumption unit in refinery and chemical enterprises. Before the 600000 ton / year aromatics unit was put into production in Hainan, all aromatics units in the world were monopolized by UOPand French IFP technology. A large amount of low temperature heat at the top of the tower and residual heat of the reaction material are used in these devices, which not only waste the low temperature heat at the top of the tower, but also consume a lot of electric energy at the same time. Sinopec Hainan Refining and Chemical Co., Ltd (abbreviated as Hainan Refining and Chemical Co., Ltd.) uses the process package technology of Sinopec's independent intellectual property rights to make a great breakthrough in energy saving and consumption reduction. On the one hand, for the tower with slightly higher top temperature in the traditional process, the steam can be produced by properly increasing the top pressure and temperature, and the steam emitted by the tower can be superheated through the convection section of the heating furnace to promote the steam turbine to generate electricity. On the other hand, for the tower with relatively low temperature at the top of the tower, a hot water exchanger is installed on the top of the tower, and the hot water is transferred to the Karina circulating hot water generation system and the ORC hot water power generation system to generate electricity after heat transfer to 120 鈩

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