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Nature Catalysis · 2021 ·Vol. 4 ·期 7 ·565-574 · IF 41.813

Room-temperature electrochemical acetylene reduction to ethylene with high conversion and selectivity

Shi Run,Wang Zeping,Zhao Yunxuan,Waterhouse Geoffrey I. N.,Li Zhenhua,Zhang Bikun,Sun Zhimei,Xia Chuan,Wang Haotian,Zhang Tierui

The selective hydrogenation of acetylene to ethylene in ethylene-rich gas streams is an important process in the manufacture of polyethylene. Conventional thermal hydrogenation routes require temperatures above 100 °C and excess hydrogen to achieve a satisfactory C 2 H 2 conversion efficiency. Here, we report a room-temperature electrochemical acetylene reduction system based on a layered double hydroxide (LDH)-derived copper catalyst that offers an ethylene Faradaic efficiency of up to ~80% and inhibits alkane and hydrogen formation. The system affords an acetylene conversion of over 99.9% at a flow rate of 50 ml min −1 in a simulated gas feed, yielding high-purity ethylene with an ethylene/acetylene volume ratio exceeding 10 5 and negligible residual hydrogen (0.08 vol.%). These acetylene conversion metrics are superior to most other state-of-the-art strategies. The findings therefore conclusively demonstrate an electrochemical strategy as a viable alternative to current technologies for acetylene-to-ethylene conversions with potential advantages in energy and atom economies.

研究领域: 化工工程 · 电化学 · 催化
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Nature Communications · 2024 ·Vol. 15 ·期 1 ·1-12 · IF 14.7

Interaction-selective molecular sieving adsorbent for direct separation of ethylene from senary C2-C4 olefin/paraffin mixture

Peng Yong,Xiong Hanting,Zhang Peixin,Zhao Zhiwei,Liu Xing,Tang Shihui,Liu Yuan,Zhu Zhenliang,Zhou Weizhen,Deng Zhenning,Liu Junhui,Zhong Yao,Wu Zeliang,Chen Jingwen,Zhou Zhenyu,Chen Shixia,Deng Shuguang,Wang Jun

Olefin/paraffin separations are among the most energy-intensive processes in the petrochemical industry, with ethylene being the most widely consumed chemical feedstock. Adsorptive separation utilizing molecular sieving adsorbents can optimize energy efficiency, whereas the size-exclusive mechanism alone cannot achieve multiple olefin/paraffin sieving in a single adsorbent. Herein, an unprecedented sieving adsorbent, BFFOUR-Cu-dpds (BFFOUR = BF 4 - , dpds = 4,4’-bipyridinedisulfide), is reported for simultaneous sieving of C 2 -C 4 olefins from their corresponding paraffins. The interlayer spaces can be selectively opened through stronger guest-host interactions induced by unsaturated C = C bonds in olefins, as opposed to saturated paraffins. In equimolar six-component breakthrough experiments (C 2 H 4 /C 2 H 6 /C 3 H 6 /C 3 H 8 /n-C 4 H 8 /n-C 4 H 10 ), BFFOUR-Cu-dpds can simultaneously divide olefins from paraffins in the first column, while high-purity ethylene ( > 99.99%) can be directly obtained through the subsequent column using granular porous carbons. Moreover, gas-loaded single-crystal analysis, in-situ infrared spectroscopy measurements, and computational simulations demonstrate the accommodation patterns, interaction bonds, and energy pathways for olefin/paraffin separations.

CAS / MDL: 67-56-1
研究领域: 化学工程 · 材料科学 · 石油化学
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