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首页> 外文期刊>Chemical Engineering Science >Extraction of ethane from natural gas at high pressure by adsorption on Na-ETS-10
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Extraction of ethane from natural gas at high pressure by adsorption on Na-ETS-10

机译:Na-ETS-10吸附从天然气中高压提取乙烷

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Methane/ethane separation was achieved using Na-ETS-10 as a packed-bed adsorbent over a pressure range of 450-5600. kPa at 298. K. At these pressures, pure methane gas raffinate streams were obtained prior to ethane breakthrough. The extract phase obtained following desorption from the packed-bed column was enriched in ethane. Extract phases containing up to 75% ethane were achieved following separations of a 93/7 methane/ethane feed mixture. Separation performance did not deteriorate as adsorption column pressures increased. Selective adsorption of a synthetic natural gas mixture using an Na-ETS-10 packed-bed column resulted in hydrocarbon outlet compositions ranging from pure methane (up to ~60 bed volumes at standard temperature and pressure) to ~93% methane, ~5% ethane and ~2% propane (~150 to ~850 bed volumes at standard temperature and pressure). In all cases, following desorption, the extract phase was highly enriched in the larger and more valuable hydrocarbons.
机译:使用Na-ETS-10作为填充床吸附剂在450-5600的压力范围内实现甲烷/乙烷分离。 kPa在298.K。在这些压力下,在乙烷突破之前获得了纯甲烷气提余液。从填充床塔解吸后获得的萃取相富含乙烷。分离出93/7甲烷/乙烷进料混合物后,可得到含最高75%乙烷的萃取相。分离性能不会随着吸附塔压力的增加而降低。使用Na-ETS-10填充床塔对合成天然气混合物的选择性吸附导致烃出口组成从纯甲烷(在标准温度和压力下高达60床体积)到93%甲烷,〜5%乙烷和约2%的丙烷(在标准温度和压力下约150至850床体积)。在所有情况下,解吸后,萃取相都高度富含较大且更有价值的烃。

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