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Benqiao He

Researcher at Tianjin Polytechnic University

Publications -  119
Citations -  3921

Benqiao He is an academic researcher from Tianjin Polytechnic University. The author has contributed to research in topics: Membrane & Chemistry. The author has an hindex of 30, co-authored 99 publications receiving 2657 citations. Previous affiliations of Benqiao He include Chinese Ministry of Education.

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Novel Functionalized Nano-TiO2 Loading Electrocatalytic Membrane for Oily Wastewater Treatment

TL;DR: This study suggests that the synergistic effect of electrocatalytic oxidation and membrane separation in the ECMR plays a key role in preventing membrane fouling in oily wastewater treatment.
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Biodiesel production using cation-exchange resin as heterogeneous catalyst

TL;DR: Three types of cation-exchange resins were employed to prepare biodiesel from acidified oils generated from waste frying oils and the results show that the catalytic activity of NKC-9 was higher than that of 001 x 7 and D61.
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Preparation and characterization of positively charged polyamide composite nanofiltration hollow fiber membrane for lithium and magnesium separation

TL;DR: In this paper, a positively charged polyamide composite nanofiltration (NF) hollow fiber membrane for lithium and magnesium separation was fabricated by interfacial polymerization of 1,4-Bis(3-aminopropyl)piperazine (DAPP) and trimesoyl chloride (TMC) on the polyacrylonitrile (PAN) ultrafiltration hollow fiber membranes.
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An Electrocatalytic Membrane Reactor with Self‐Cleaning Function for Industrial Wastewater Treatment

TL;DR: This work presents the design of a novel electrocatalytic membrane reactor (ECMR) with self-cleaning function, and proposes a simple strategy that could avoid membrane fouling completely in industrial water treatment.
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A continuous process for biodiesel production in a fixed bed reactor packed with cation-exchange resin as heterogeneous catalyst

TL;DR: NKC-9 resin shows the potential commercial applications to esterification of FFA and its results showed that the FFA conversion increased with increases in methanol/oil mass ratio, reaction temperature and catalyst bed height, whereas decreased with increase in initial water content in feedstock and feed flow rate.