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案件記録

Membrane Concentration of Dissolved Species

発明審査中
2閲覧数
11請求項 · 2 独立
§ Ⅰ

案件概要

発明者

Siva Kumar Kota; Hiep Le; Chun Yew Chong

IPC分類

B1D 61/2C1C 1/24C2F 1/44C2F 1/52C2F 101/10C2F 101/20C2F 103/10C22B 3/C22B 3/22C22B 3/44

CPC分類

B1D61/26C1C1/24C2F1/441C2F1/5236C22B3/22C22B3/44C22B23/461B1D2315/24B1D2317/6C2F2101/101C2F2101/20C2F2103/10

A dissolved species (e.g., sulfur) is concentrated from a feed liquid by passing the feed liquid into a first reverse-osmosis module of a first reverse-osmosis assembly, where the feed liquid is separated with a membrane to produce a permeate and a concentrate solution. In a de-supersaturation module, dissolved components are precipitated from the concentrate solution to produce solid precipitates and a de-supersaturated concentrate solution, which is passed to a second reverse-osmosis assembly, where the de-supersaturated concentrate solution is separated with a membrane to produce a permeate and a concentrated brine. In a polishing module, the permeates from the first and second reverse-osmosis assemblies are further purified to produce a polished permeate and a concentrate solution that is recycled back to the retentate side of the first reverse-osmosis module of the first reverse-osmosis assembly where it mixes with the feed liquid, and the polished permeate is extracted from the polishing module.

原文(中国語)

A dissolved species (e.g., sulfur) is concentrated from a feed liquid by passing the feed liquid into a first reverse-osmosis module of a first reverse-osmosis assembly, where the feed liquid is separated with a membrane to produce a permeate and a concentrate solution. In a de-supersaturation module, dissolved components are precipitated from the concentrate solution to produce solid precipitates and a de-supersaturated concentrate solution, which is passed to a second reverse-osmosis assembly, where the de-supersaturated concentrate solution is separated with a membrane to produce a permeate and a concentrated brine. In a polishing module, the permeates from the first and second reverse-osmosis assemblies are further purified to produce a polished permeate and a concentrate solution that is recycled back to the retentate side of the first reverse-osmosis module of the first reverse-osmosis assembly where it mixes with the feed liquid, and the polished permeate is extracted from the polishing module.

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