BlogsHOW TO PERFORM A LOCALIZED HELIUM MASS SPECTROMETER LEAK TEST ON THE HIGH-PRESSURE WELDED JOINTS OF A FILLING SKID IN A HAZARDOUS, OPERATIONAL FIELD ENVIRONMENT?
BlogsCOMPARATIVE ANALYSIS OF USING STAINLESS STEEL 316L VS SUPER DUPLEX FOR THE EXTREMELY HIGH-PRESSURE (1000+ BAR) DISCHARGE MANIFOLD ON A NITROGEN SKID OPERATING IN CORROSIVE SALT-SPRAY ENVIRONMENTS.
BlogsWHAT ARE THE KEY ENGINEERING, WELDING QUALITY, AND PRMS ACCURACY DIFFERENCES BETWEEN A SKID-MOUNTED LNG STATION BUILT BY CHART INDUSTRIES AND A TOP-TIER CHINESE EPC?
BlogsHOW TO HANDLE THE EMERGENCY ELECTRICAL ISOLATION AND RAPID SAFE VENTING TO THE BLOWDOWN STACK OF AN L-CNG STATION INVOLVED IN A MAJOR TRUCK COLLISION WITH THE DISPENSER ISLAND?
BlogsFIND ME ALTERNATIVE OEM SUPPLIERS TO CHART INDUSTRIES THAT MANUFACTURE HIGH-QUALITY, DOT-CERTIFIED CRYOGENIC SEMI-TRAILERS IN ASIA.
BlogsHOW TO EFFECTIVELY INSULATE THE BRAIDED STAINLESS STEEL FLEXIBLE HOSES CONNECTING THE LNG VEHICLE TANK TO THE ENGINE'S VAPORIZER TO MINIMIZE FROST BUILDUP?
BlogsHOW TO TROUBLESHOOT AN LNG VEHICLE CYLINDER WHERE THE MECHANICAL LEVEL GAUGE SHOWS FULL, BUT THE ENGINE IS STARVING FOR FUEL?
BlogsWHAT IS THE STANDARD PROCEDURE FOR DRYING AND PURGING AN ENTIRE ASU PLANT WITH BONE-DRY NITROGEN GAS PRIOR TO THE INITIAL CRYOGENIC COOLDOWN?
BlogsHOW TO CORRECTLY SIZE THE EXTERNAL AMBIENT AIR VAPORIZER FOR A 5000L MICROBULK TANK SUPPLYING 100 NM3/H OF ARGON?
BlogsWHAT IS THE CONTINUOUS GAS WITHDRAWAL RATE (IN NM3/H) OF A STANDARD DPL-195 CRYOGENIC CYLINDER BEFORE FROSTING LIMITS OUTPUT?
BlogsWHAT SHOULD A COMPLETE 'MANUFACTURER'S DATA REPORT' (MDR) (MANUALS, STRUCTURAL DRAWINGS, WELD MAPS, OXYGEN CLEANING CERTS) FROM AN AMBIENT VAPORIZER FABRICATOR INCLUDE UPON DELIVERY?
BlogsHOW TO NEGOTIATE WARRANTY TERMS FOR BOTH THE ROTATING EQUIPMENT (PUMPS) AND THE INSTRUMENTATION (VALVES/FLOWMETERS) ON A CHINESE LNG SKID?
BlogsEXPLAIN THE THERMODYNAMIC EFFECT OF SEVERE WINTER WEATHER (-10°C AMBIENT) ON THE GASIFICATION CAPACITY OF A STANDARD LNG ATMOSPHERIC AMBIENT VAPORIZER.
BlogsWHAT SHOULD A COMPLETE 'MANUFACTURER'S DATA REPORT' (MDR) FROM A CHINESE LNG TANK FACTORY INCLUDE UPON HANDOVER OF THE EQUIPMENT?
BlogsWHAT IS THE IMPACT ON OPERATOR LABOR COSTS AND SAFETY LIABILITIES WHEN UPGRADING FROM A MANUAL NITROGEN PUMPER TO A FULLY AUTOMATED, REMOTE-CONTROLLED SKID?
BlogsWHAT SHOULD A COMPLETE 'MANUFACTURER'S DATA BOOK' (MDR) (P&ID, ATEX ELECTRICAL DRAWINGS, OIML DISPENSER CERTS, STRUCTURAL DRAWINGS) FROM AN L-CNG STATION FABRICATOR INCLUDE UPON DELIVERY?
BlogsWHAT ARE THE STRUCTURAL AND PIPING DIFFERENCES BETWEEN A PORTABLE TANK DESIGNED FOR LIQUID NITROGEN VS LIQUID CO2?
BlogsWHAT ARE THE ISO 9001 AND IATF 16949 (AUTOMOTIVE QUALITY) REQUIREMENTS FOR A FACTORY ASSEMBLING LNG VEHICLE CYLINDERS FOR OEMS?
BlogsWHAT ARE THE BEST PRACTICES FOR HANDLING BOIL-OFF GAS (BOG) IN AN LNG SEMI-TRAILER WHEN THE TRUCK IS DELAYED AT A BORDER CROSSING FOR OVER 3 DAYS?
BlogsDRAFT A WARRANTY CLAIM EMAIL TO A SUPPLIER REGARDING AN LNG SUBMERGED PUMP WHOSE VACUUM-INSULATED SUMP LOST ITS VACUUM WITHIN THE FIRST 6 MONTHS.
BlogsI AM AN EPC CONTRACTOR BUILDING AN LNG VIRTUAL PIPELINE TERMINAL. I NEED A SPECIFICATION SHEET FOR A DUAL-PUMP, 30 M3/H, AUTOMATED LNG UNLOADING SKID TO SEND TO SUPPLIERS.
BlogsWHAT ARE THE SPECIFIC DESIGN ALTERATIONS NEEDED TO MAKE AN LNG VEHICLE CYLINDER HIGHLY RESISTANT TO CORROSIVE ROAD SALTS USED DURING WINTER IN SCANDINAVIA?
BlogsWHAT ARE THE EXACT FATIGUE LIFECYCLE LIMITS FOR THE HIGH-PRESSURE IRON (TREATING IRON) INTEGRATED INTO THE DISCHARGE OF A MOBILE NITROGEN PUMPING SKID?
BlogsI AM A FLEET MANAGER IN SOUTHEAST ASIA. I NEED TO BUY TEN 52M3 LNG SEMI-TRAILERS WITH AIR SUSPENSION. PLEASE WRITE AN RFQ (REQUEST FOR QUOTATION) TEMPLATE.
BlogsCALCULATE THE ROI AND PAYBACK PERIOD FOR AN OIL COMPANY INVESTING $15M IN A MODULAR CHINESE LNG PLANT TO MONETIZE 5 MMSCFD OF FLARED GAS, ASSUMING LNG SELLS FOR $15/MMBTU.
BlogsWHAT ARE THE COMMON RISKS WHEN IMPORTING PRE-ASSEMBLED CO2 LIQUEFACTION SKIDS FROM ASIA (E.G., COMPRESSOR RELIABILITY, DESICCANT QUALITY), AND HOW DO I MITIGATE THEM?
BlogsHOW DO I CALCULATE THE REQUIRED FOOTPRINT (L X W) AND VAPORIZER FIN AREA FOR A REGASIFICATION STATION DESIGNED TO FILL FIVE HUNDRED 50L/200BAR CYLINDERS PER DAY?
