Issues regarding the testing of pipe fittings for highly hazardous media – Core principles. When dealing with highly hazardous media such as HF, H₂S, chlorine, phosgene, etc., the core principles are: the highest standards in design, the strictest testing procedures, and the most conservative testing methods, all to ensure absolute safety and sealing performance and to prevent catastrophic leaks. 1. Regarding Non-Destructive Testing (NDT): Yes, it is generally required to have at least two 100% surface inspections, with the methods being complementary to each other. First step (root inspection): It is generally required to conduct 100% magnetic particle testing (MT) or penetrant testing (PT) immediately after welding is completed. The purpose is to detect minor defects on the surface and near the surface of welds, such as cracks, lack of fusion, pores, etc., as early as possible before heat treatment and any pressure testing. For magnetic materials, magnetic particle testing (MT), which has higher sensitivity, is preferred. Second step (final inspection): After all manufacturing processes (such as post-weld heat treatment PWHT and pressure testing) are completed, 100% magnetic particle testing (MT) or penetrant testing (PT) is carried out again. This is because new stress cracks may arise or existing minor defects may expand during heat treatment and pressure testing, so final verification is necessary. Additional note: The necessity of RT (radiographic testing): For critical pipelines, in addition to surface inspection, 100% radiographic testing (RT) or ultrasonic testing (UT) of the weld joints is usually required. RT/UT are primarily used to detect volumetric defects inside welds (such as pores and slag inclusions) as well as surface defects (such as lack of penetration and incomplete fusion). Therefore, a complete NDT program is usually a combination of “100% RT/UT + 100% MT/PT”. Compliance with standards: The specific testing ratios and methods must comply with the design documents, customer specifications, as well as relevant international/**standards (such as ASME B31.3 Process Piping, GB/T 20801, etc.). Conclusion: The approach you mentioned of \"conducting at least two inspections, with 100% surface inspection for each\" is a common and correct practice, but it is usually used in combination with volume inspection (RT/UT). 2. Local heat treatment of pipe fittings is difficult to carry out, but it is usually necessary and requires very high standards. Why must it be done? Stress relief: Welding generates significant residual stresses, and for highly hazardous media, stress corrosion cracking (SCC) is one of the main risks. Post-weld heat treatment (PWHT) is the most effective method for eliminating residual stresses. Improving microstructure: Heat treatment can temper the rough hardened structure, thereby enhancing the toughness and mechanical properties of the weld area. Why is it “not easy”? Temperature control: Very precise heating temperatures, rates of temperature increase/decrease, and holding times are required, which imposes high demands on both the equipment and the operators. Uniformity: Achieving uniform heating around the entire weld perimeter and in its cross-section is a technical challenge; uneven temperatures can lead to new problems. On-site constraints: Local heat treatment on an installed piping system involves the presence of other equipment, insulation, or cables in the vicinity, which requires proper protection and isolation; this increases the difficulty and risks of the work. How to do it well? Professional electric heating elements and an intelligent temperature control system are used. Follow the requirements of the WPS (Welding Procedure Specification) and PQR (Process Qualification Record) strictly. Place a sufficient number of thermocouples around the heating area to monitor the temperature in real time and keep records. Operated by qualified personnel and teams. Conclusion: This is a technically complex and costly process, but for pipelines carrying highly hazardous media, it is usually a mandatory requirement; the standards cannot be waived or reduced just because it is difficult to implement. 3. Regarding the leakage tests for the tube side and shell side, strict leakage tests must be conducted on each of them separately. Tube Side: It is in direct contact with highly hazardous media; its integrity is of primary importance, and leak tests must be conducted. Shell Side: Equally crucial. Risk 1: If the tube side fluid leaks into the shell side (e.g., cooling water), it will lead to a leakage of the fluid, resulting in safety accidents and environmental pollution. Risk 2: If the shell-side fluid leaks into the tube side (although this is less common, it depends on the design), it can also cause problems. Regulatory requirements: Pressure vessel codes such as ASME SEC VIII DIV 1 specify clear testing requirements for the tube ends and tube sheet joints of heat exchangers. Test method: First, a pressure test (Hydrostatic Test / Pneumatic Test) is conducted: this is a strength test aimed at verifying the overall strength and airtightness of the pressure-bearing components. The tube side and shell side must be tested using separate test pressures. Then a sensitivity leak test is conducted: after the pressure test, an even more sensitive leak test is performed to detect extremely minor leaks. This is what you asked about in point 4. 4. Selection of leakage testing methods (for extremely hazardous media such as HF) For extremely hazardous media with high permeability like HF (hydrogen fluoride), standard airtightness tests are far from sufficient. The most sensitive leak detection method must be used. Air Tightness Test: It has low sensitivity and can usually only detect larger leaks (>10⁻³ ~ 10⁻⁴ Pa·m³/s). It must never be used as the final leak test method for HF medium pipelines. Ammonia Leak Test: It has higher sensitivity than the airtightness test, but it still has limitations (on the order of about 10⁻⁵ Pa·m³/s). Moreover, ammonia is corrosive in itself and may react with residues in the system; it is not suitable for certain materials such as copper alloys. Helium Mass Spectrometry Leak Detection: This is the gold standard and the preferred choice for highly hazardous media such as HF. Principle: Helium is used as a tracer gas, and a helium mass spectrometer leak detector is employed for detection in external vacuum or suction mode. Helium molecules are small, inert, non-toxic, and do not contaminate the product. Moreover, leak detectors have extremely high sensitivity, ranging from 10⁻¹¹ to 10⁻¹² Pa·m³/s, allowing them to detect even the tiniest leaks at the molecular level. Method: Vacuum method: Evacuate the system (or a local space) and spray helium gas from the outside. Sniffing Mode: A helium gas mixture at a certain pressure is introduced into the system, and an external sniffing probe is used to scan all welds, flanges, valves, and other sealing points. Special note regarding HF gas: HF molecules are small and highly corrosive, and can easily leak through gaps that are invisible to the naked eye. Helium mass spectrometry leak detection must be used to ensure absolute certainty. In the specifications for many international projects (such as the petrochemical and semiconductor industries), helium testing is mandatory for HF media. Summary and Recommendations: Testing: Adopt a testing strategy that combines 100% RT/UT + 100% MT/PT. Heat treatment: Must be done. Allocate the necessary resources, and have a professional team carry out precise operations using qualified equipment. Test scope: Both the tube side and the shell side must undergo pressure testing and sensitivity leakage testing separately. Leak testing method: For HF media, the airtightness test is omitted, and helium mass spectrometry leak detection is used as the mandatory final acceptance criterion. The final decision must be based on: the project design specifications, the client’s requirements, and the mandatory engineering standards to be followed (such as ASME, GB, EN, etc.). Before carrying out any work, it is essential to conduct a thorough process safety analysis (such as HAZOP, LOPA, etc.) and develop a comprehensive quality inspection plan (ITP). All steps must be approved by the client and third-party inspection agencies.