Breaking through the theoretical framework and bottleneck that traditional high-temperature corrosion inhibitors can only use phosphorus-based systems, it provides good corrosion inhibition under vacuum conditions at 220~360℃, and avoids fouling, blockage and unplanned shutdowns of downstream units such as hydrotreating caused by phosphorus-containing high-temperature inhibitors.
| Project | Technical Indicators | Testing Standards/Methods |
|---|---|---|
| Appearance | Uniform tan liquid | Visual inspection |
| Solubility | Miscible with aromatic hydrocarbons in any ratio | Visual inspection |
| Density (20℃), g/cm³ | 0.80~1.00 | GB/T 2540 |
| Freezing point, ℃ | ≤-10 | GB/T 510 |
| Closed cup flash point, ℃ | ≥61 | GB/T 261 |
| Phosphorus content, % | ≤0.01 | SH/T 0296-1992 |
| Chloride ion content, % | ≤0.01 | ASTM D7536 |
| Corrosion inhibition rate, % | ≥90 | Q/WRUN002-2019 |
When the feedstock acid value is ≥0.5 mgKOH/g and the temperature exceeds 200°C, it is strongly recommended to choose BXH-103/RUN-129 instead of ordinary phosphorus-containing high-temperature inhibitors, addressing both high-temperature corrosion and the impact of phosphorus on oil quality.
Residue oil system at the bottom of the pressure reduction tower, 250–320°C high temperature oil and gas corrosion environment
High temperature and high pressure hydrogen environment, NH₄HS·HCl compound corrosion conditions
Delayed coking high-temperature oil and gas pipelines containing H₂S·Organic acid corrosion
Park refinery with zero phosphorus emission requirements, replacing phosphorus-containing high-temperature corrosion inhibitors
Ordinary imidazoline corrosion inhibitors lose their protective effect due to the breakage of adsorption bonds when the temperature is above 150°C. FCC In high-temperature devices such as catalytic cracking, vacuum coking, and residual oil hydrogenation, the operating temperature is generally 200–350°C. At the same time, the concentration of the corrosive medium (naphthenic acid·H₂S·HCl) is high, and the corrosion rate can be as high as 2–5 mm/a. By introducing a highly thermally stable heterocyclic structure, BXH-103 extends the effective operating temperature to 300°C, filling the product gap in the field of high-temperature corrosion inhibition.
Under high-acid crude processing conditions (TAN>1.0 mgKOH/g), BXH-103/RUN-129 is applied to vacuum residue lines and high-temperature heat exchangers with an acceptance criterion of ≥90% inhibition (finished product, Q/SHCG standards). Successfully trialed at a coastal refinery No.2 CDU (signed application report, verified by the client group research institute scale-sample analysis), with an evaluation certificate issued by A Central China refinery.
| index | numerical value |
| Appearance | Dark brown homogeneous liquid |
| Phosphorus content | Not detected (<0.01%) |
| Use temperature | 80–300℃ (can withstand 350℃ in the short term) |
| Recommended dosage | 15–50 mg/L |
| Naphthenic acid corrosion inhibition | TAN≤4.0 mgKOH/g device is applicable |
| Implementation standards | Q/BXH 003—2023 |
BXH-103 is for high temperature working conditions FCC Corrosion inhibitor for equipment, suitable for naphthenic acid and sulfur corrosion protection in FCC oil slurry circulation lines, vacuum coking, residual oil hydrogenation and other high-temperature parts above 220℃.
BXH-103 / RUN-129 solve the two major problems of high temperature corrosion and environmental protection standards for you at the same time