计算机与应用化学
計算機與應用化學
계산궤여응용화학
COMPUTERS AND APPLIED CHEMISTRY
2013年
3期
330-334
,共5页
曹俊雅%曾齐斌%李媛媛%白媛媛%何璐
曹俊雅%曾齊斌%李媛媛%白媛媛%何璐
조준아%증제빈%리원원%백원원%하로
合成气%Aspen Adsorption%变压吸附%羰基化%加氢
閤成氣%Aspen Adsorption%變壓吸附%羰基化%加氫
합성기%Aspen Adsorption%변압흡부%탄기화%가경
syngas%Aspen Adsorption%pressure swing adsorption%carbonylation%hydrogenation
随着合成气制备工艺的迅速发展,提纯合成气中的有用成分应用于工业生产愈显重要。本研究将含有 CO、H2、CH4、H2O、CO2及少量烃类的粗合成气经过变压吸附提纯后作为与丁烯反应生产2-丙基庚醇的原料气。该变压吸附过程包含2段,第一段采用装载硅胶和活性炭的复合床层用以脱去除 H2与 CO 以外的其他气体获得较纯的合成气;第二段采用装载 NA 型络合吸附剂的床层用以分离 H2和 CO。利用 Aspen Adsorption 软件对变压吸附过程进行了模拟。模拟结果表明,采用该2段变压吸附过程可以获得纯度为99.9%的 H2用于烯醛加氢反应,同时由二段吸附过程的解吸气可配出 H2:CO=1:1的混合气用于丁烯羰基化反应。
隨著閤成氣製備工藝的迅速髮展,提純閤成氣中的有用成分應用于工業生產愈顯重要。本研究將含有 CO、H2、CH4、H2O、CO2及少量烴類的粗閤成氣經過變壓吸附提純後作為與丁烯反應生產2-丙基庚醇的原料氣。該變壓吸附過程包含2段,第一段採用裝載硅膠和活性炭的複閤床層用以脫去除 H2與 CO 以外的其他氣體穫得較純的閤成氣;第二段採用裝載 NA 型絡閤吸附劑的床層用以分離 H2和 CO。利用 Aspen Adsorption 軟件對變壓吸附過程進行瞭模擬。模擬結果錶明,採用該2段變壓吸附過程可以穫得純度為99.9%的 H2用于烯醛加氫反應,同時由二段吸附過程的解吸氣可配齣 H2:CO=1:1的混閤氣用于丁烯羰基化反應。
수착합성기제비공예적신속발전,제순합성기중적유용성분응용우공업생산유현중요。본연구장함유 CO、H2、CH4、H2O、CO2급소량경류적조합성기경과변압흡부제순후작위여정희반응생산2-병기경순적원료기。해변압흡부과정포함2단,제일단채용장재규효화활성탄적복합상층용이탈거제 H2여 CO 이외적기타기체획득교순적합성기;제이단채용장재 NA 형락합흡부제적상층용이분리 H2화 CO。이용 Aspen Adsorption 연건대변압흡부과정진행료모의。모의결과표명,채용해2단변압흡부과정가이획득순도위99.9%적 H2용우희철가경반응,동시유이단흡부과정적해흡기가배출 H2:CO=1:1적혼합기용우정희탄기화반응。
It is more and more important to purify useful components from syngas for industrial production with the rapid development of the syngas preparation technology. In this study, the crude syngas consisted of CO, H2, CH4, H2O, CO2 and a small amount of hydrocarbon gas was purified by the pressure swing adsorption (PSA), and the purified gas was used as the row gas in a reaction with butylenes for the production of 2-propyl heptanol. This PSA process includes two stages: a layered bed loaded silicone and activated carbon used as adsorbents to removal all the compositions except H2 and CO in the first stage; a single bed loaded NA used as adsorbents to separate H2 and CO in the second stage. PSA process was simulated by Aspen Adsorption software. Simulation results indicate that after these two stages of PSA, the H2 with the purity of 99.9% can be obtained for the hexenal hydrogenation reaction. On the other hand, the mixture gas for the carbonylation of butylenes can be obtained by adding the purified H2 to the desorbed gas from the second stage obtains.