Clarification of Furnace Gas Cleaning Circulating Water Using Cationic Flocculant

2024

Closed access Metadata (CSL-JSON)
DOI 10.3103/s0967091224701791
Data confidence 70 medium
How this score is calculated

It is built from checkable properties of the record itself: whether the article has a DOI, how many independent sources confirmed its data, whether the required fields are filled in, and how recent the latest confirmation is. Disagreement between sources and a missing identifier lower it. A value of 80 or above means the record was published without further checking; 60 to 79 means it is published at reduced confidence, with a manual check advisable. A record verified by an editor by hand is never pushed below 90 by a recalculation. This scores our data about the article, not the article itself.

Abstract

The article presents the results of laboratory testing to select the optimal flocculant for clarification of circulating water from the shaft furnace gas cleaning of the metallization department. Laboratory testing was carried out using the standard settling (clarification) technique in sedimentation glasses. It is shown that the use of a liquid emulsion flocculant with a low cationic charge and high molecular weight allows for the successful removal of suspended and colloidal substances from the circulating water of the gas cleaning system and ensures the quality of the clarified water corresponding to the standard for the content of suspended substances ≤30 mg/dm3. It is established that the optimal dosing point for the selected liquid emulsion flocculant is a zone of high turbulence and intensive mixing, i.e., the receiving chamber of the radial-flow settling tank. The proposed reagent treatment program is recommended for industrial use for clarification of shaft furnace gas cleaning circulating water of one of the metallurgical plants in Russia. The optimal dosage range of the selected cationic flocculant (according to the commercial reagent) based on the wastewater entering the radial-flow settling tank is 0.4–0.5 g/m3.