Specifying a Fibrous-Ball Filter: Compression Mode, Backwash Method and Effluent Oil Targets

Specifying a Fibrous-Ball Filter: Compression Mode, Backwash Method and Effluent Oil Targets

2026-09-16

A practical specification guide for high-efficiency fibrous-ball filters in oilfield and refining service, covering modified hydrophilic-oleophobic media, hydraulic versus mechanical compression, gas-water backwash and performance limits.

Super-Gravity Against Gravity Settling: What a High-Efficiency Hydrocyclone Removes at 10 Microns

Super-Gravity Against Gravity Settling: What a High-Efficiency Hydrocyclone Removes at 10 Microns

2026-09-16

How super-gravity cyclonic separation outperforms conventional gravity oil removers in refinery and oilfield pretreatment, with design logic, performance parameters and a head-to-head comparison table.

Inside KLE-HEC-200: How a Multi-Metal Ozone Catalyst Handles COD 200-2000 mg/L Without Clogging

Inside KLE-HEC-200: How a Multi-Metal Ozone Catalyst Handles COD 200-2000 mg/L Without Clogging

2026-09-16

An engineering assessment of the KLE-HEC-200 heterogeneous ozone catalyst, covering its multi-metal catalytic mechanism, core performance indicators, four project case studies and where it fits alongside CDFU and CDOF equipment.

Eight Engineering Reasons Ultra-Fine SIC Membrane Filters Survive Where Organic Media Fail

Eight Engineering Reasons Ultra-Fine SIC Membrane Filters Survive Where Organic Media Fail

2026-09-16

A breakdown of the eight design traits that let ultra-fine SIC inorganic silicon-carbide membrane filters handle hot, corrosive and oily industrial wastewater that destroys organic and ordinary ceramic membranes.

Why SiC Ceramic Membranes Beat PVDF in Oily Wastewater Reuse: A Practical Selection Guide

Why SiC Ceramic Membranes Beat PVDF in Oily Wastewater Reuse: A Practical Selection Guide

2026-09-16

A field-oriented look at why silicon carbide ceramic membranes outlast PVDF and conventional ceramics in oily wastewater polishing, covering flux, temperature limits, fouling behaviour and where the unit sits in a reuse train.

Total Solids Explained: Why the Drying Temperature Decides the Number You Report

Total Solids Explained: Why the Drying Temperature Decides the Number You Report

2026-09-15

What total solids actually measures, how 103-105 degrees C and 180 plus minus 2 degrees C drying give different answers, and how TS splits into dissolved, suspended, volatile and fixed fractions.

Depot Drain Water Carries Gasoline: Recovering Product While Meeting Reuse Limits

Depot Drain Water Carries Gasoline: Recovering Product While Meeting Reuse Limits

2026-09-15

Why light-oil depot drain water has to be treated as both an environmental and a resource problem, and how a fully enclosed CDFU plus KHC coalescing oil separator train recovers gasoline while producing reusable wash water.

Walnut Shell Absorbs, SFM Repels: Rethinking Media for Oily Wastewater Polishing

Walnut Shell Absorbs, SFM Repels: Rethinking Media for Oily Wastewater Polishing

2026-09-15

A point-by-point comparison of SFM super-hydrophilic modified active filter media against walnut-shell media: contact angle, hydration layer, backwash behaviour, precision, service life and hazardous-waste burden.

Configure by Pollutant Form, Not by Total Number: Routing Logic for Hard Wastewater

Configure by Pollutant Form, Not by Total Number: Routing Logic for Hard Wastewater

2026-09-15

Why total oil or total COD tells you nothing about the right process, how five pollutant forms map onto SINOKLE's coalescing, CDFU, CDOF and KFM units, and what the Xinjiang and Congo-Brazzaville projects achieved.

Condensate Water and the Micro-Oil Problem: Why CDFU + SFM Beats Settling and Sand

Condensate Water and the Micro-Oil Problem: Why CDFU + SFM Beats Settling and Sand

2026-09-15

Why gravity settling, ordinary DAF and quartz-sand filtration miss micron-scale emulsified oil in oilfield condensate water, and how a CDFU plus SFM high-precision filter pair handles flow swings and trace oil.