20 years of petrochemical refining practice accumulation, covering the entire process of atmospheric and vacuum distillation, catalytic cracking, hydrogenation and coking
Crude oil contains HCl (main source: hydrolysis of organic chlorides), H₂S and organic acids. During the distillation process, highly corrosive liquids are formed in the gas phase condensation area at the top of the tower, which is the core control area of the refinery's "one removal and four injections". Typical corrosion rates can reach >1 mm/a, causing frequent heat exchanger leaks and tower top pipeline perforation accidents.
use BXH-101 Water-soluble corrosion inhibitor Inject wash water at the top of the tower (recommended concentration 20–50 mg/L), with BXH-102 Oil-soluble imidazoline intermediate Inject side-line distillate oil (10–30 mg/L) to form a water phase and oil phase dual-channel protection system. The target corrosion rate is reduced to 0.05–0.10 mm/a (industry excellent level).
Vacuum residue treatment and high-temperature hydrogenation reactor effluent system (250–320°C) exceed the temperature limit of ordinary imidazoline corrosion inhibitors. At the same time, many provincial parks will implement strict phosphorus content emission standards from 2026, and traditional phosphorus-containing high-temperature corrosion inhibitors face compliance risks.
use BXH-103/RUN-129 Phosphorus-free high temperature corrosion inhibitor, the phosphorus content is <0.001%, and the film formation integrity rate is >85% under 300°C working conditions. It simultaneously solves the two major pain points of high-temperature corrosion protection and environmental compliance without additional wastewater treatment costs.
| Plan | Applicable Temperature | Phosphorus Content |
|---|---|---|
| Ordinary imidazoline | ≤180°C | Phosphorus-free |
| Phosphorus high temperature agent | ≤280°C | High phosphorus |
| BXH-103 | ≤300°C | Phosphorus-free✔ |
As refinery feedstocks become heavier and lower in quality, demand for coker gas oil denitrification keeps growing. Benxin applies a non-hydrogenation complexation process, backed by 13 national patents, with full support from lab trials to on-site engineering service. View the full denitrification solution →
Non-hydrogenation complexation denitrification project (tank settling process): reduces basic nitrogen and improves FCC feed quality.
Measured results: basic nitrogen reduced from 1136/1585 μg/g to 429.8/772.5 μg/g at ~1.0-1.1% dosage.
Click to view the technical details and measured data of real refinery applications and project plans.
High-temperature naphthenic acid corrosion inhibition, the second normal device was successfully tested and verified by scale sample analysis of CNOOC Research Institute.
View case →Non-hydrogenation complex denitrification tank area settlement process project plan to improve the feed quality of coked wax oil catalytic cracking.
View case →The measured alkali nitrogen in Changyi/Qingzhou is 1136/1585→429.8/772.5 μg/g, and the acid value after removal is as low as 0.15 mgKOH/g.
View case →20 years of experience in petrochemical refining services, free technical consultation, quick response
Hubei Benxin Environmental Protection Technology corrosion inhibitor products are already available in Sinopec (SINOPEC), China National Offshore Oil Corporation (CNOOC), China National Petroleum Corporation (CNPC), Dongming Petrochemical, extend oil, BEFAR GROUP, SINOCHEM ENERGY Wait Large refining and chemical companies Normal and vacuum distillation, catalytic cracking, delayed coking Stable application in core devices such as Through strict on-site evaluation and long-term operation verification.







