English — Forum #336 (Page 18/51)
- How can the thermal conductivity of anhydrous sulfuric acid solution be estimated or looked up? - HCBBS Forum
- A big horse can’t pull a small cart - HCBBS Forum
- Calculation table for packed absorption towers (suitable for rapid irreversible chemical absorption) - HCBBS Forum
- Ammonia purification in acidic water stripping unit - HCBBS Forum
- Request the line pattern or legend for the SIS to DCS signal transmission cable - HCBBS Forum
- Questions about safety valve pipeline settings - HCBBS Forum
- Guidelines for the Implementation of Equipment Integrity Management and Predictive Maintenance Systems in the Safe Production of Hazardous Chemicals (Trial Version) - HCBBS Forum
- Seek help regarding “Granulation Tower and Granulation Nozzles” - HCBBS Forum
- There may be misunderstandings regarding the total volume of combustible gas storage tanks as specified in petrochemical standards - HCBBS Forum
- Seeking \"Modern Pump Theory and Design\" - HCBBS Forum
- What are the potential hazards of introducing both circulating water and steam at the lower outlet of the reactor jacket? - HCBBS Forum
- The outlet pressure of the waterway pressure reducing valve cannot be adjusted, why (the outlet pressure cannot be adjusted to 1 Bar) - HCBBS Forum
- I would appreciate it if colleagues from engineering companies or design institutes could help answer this - HCBBS Forum
- What is the process of filling a steam drum with water? - HCBBS Forum
- Is it okay to have a level gauge without a flow meter? - HCBBS Forum
- Spacing requirements between liquid ammonia storage tanks and other equipment - HCBBS Forum
- I need everyone’s help to determine the length of the spacing tube - HCBBS Forum
- Under what circumstances is it necessary to install a safety valve? - HCBBS Forum
- Piping single-line diagram/axonometric view — Mobile measurement & on-site drawing for quantity calculation - HCBBS Forum
- 3D factory design software series for chemical projects----PDS series - HCBBS Forum
- What is the saturated vapor pressure of hydrochloric acid at 60~80°C? - HCBBS Forum
- The purpose of installing a bypass check valve at the PSV inlet of the reactor vessel - HCBBS Forum
- What category does sodium hydroxide fall into in HGT20660? - HCBBS Forum
- 【Haichuan Equipment Guessing Game】Whose twin towers? - HCBBS Forum
- Hydrogen and air are combined and released - HCBBS Forum
- Issues regarding the plant location and layout of the plant area (downwind side or upwind side) - HCBBS Forum
- No steam ejectors for sulfur recovery! - HCBBS Forum
- Effect of the stripping tower top pressure on the stripping efficiency - HCBBS Forum
- Is the fire hazard of the Klaus sulfur recovery unit classified as Class A or Class D? - HCBBS Forum
- Technology transfer for sodium chloride electrolysis - HCBBS Forum
- Design the pump outlet venting method - HCBBS Forum
- Seeking expert help with gas pipeline pressure drop calculation - HCBBS Forum
- Temperature groups T1~T5? - HCBBS Forum
- Is it necessary to install backup storage tanks in the liquefied hydrocarbon storage area? - HCBBS Forum
- BDV valve for liquefied gas cylinders - HCBBS Forum
- Recommended for sharing: Some experiences in the design of static equipment for an EPC project in the petrochemical industry - HCBBS Forum
- Regarding the control of the cut-off valve - HCBBS Forum
- Must pressure vessels be equipped with safety valves or rupture discs? - HCBBS Forum
- Series of 3D factory design software for chemical projects----Smart 3D series - HCBBS Forum
- Discussion on whether the low-point nitrogen purge pipeline can be blown clean - HCBBS Forum
- Can telecommunication cables and power cables be placed inside the same protective steel tube? - HCBBS Forum
- In areas where hydrogen pipelines pass through, does the explosion-proof rating of all electrical equipment need to be upgraded? - HCBBS Forum
- Keeping up with the times? ? Are project names becoming more and more fancy and confusing these days? - HCBBS Forum
- Why isn’t white phosphorus considered a highly toxic substance? - HCBBS Forum
- Regarding the cost of main materials in the process estimate - HCBBS Forum
- Material of electrolyte pipelines for all-vanadium flow batteries - HCBBS Forum
- What is tube toothing in heat exchange tubes? - HCBBS Forum
- SH/T3098-2011 Calculation of Support Beams for Internal Components in Towers (Simply Supported Beams) - HCBBS Forum
- Lao K chemical design technical services and consulting content - HCBBS Forum
- In which standard are the concepts of Class A, Class B, and Class C workshops mentioned? - HCBBS Forum
- Carrying out all chemical-related experiments - HCBBS Forum
- Pressure pipeline - HCBBS Forum
- Explanation of the calculation table for fluid and gas pipeline pressure drop - HCBBS Forum
- DEP 31.38.01.26 Hello, experts – I need help with this Shell file - HCBBS Forum
- Pre-cooling before LNG cold box - HCBBS Forum
- Overall location of the sewage treatment plant - HCBBS Forum
- On the qualitative assessment of the fire hazard in waste gas and wastewater treatment plants - HCBBS Forum
- Dear colleagues, does anyone have the design specification for a fluidized bed dryer (air flow drying)? - HCBBS Forum
- Where can I find information on the physical properties of glucose? - HCBBS Forum
- Interpretation of the layout specifications for steam pipeline branches - HCBBS Forum
- Container pressure experiment - HCBBS Forum
- Contract signed for EPC general contracting of the world’s largest integrated green hydrogen, ammonia, and alcohol project - HCBBS Forum
- Can fluorinated lining pipes transport chlorine? - HCBBS Forum
- Issues regarding the substitution of nickel-based alloy materials - HCBBS Forum
- Calculate the heat of synthesis of ethylenediamine hydrochloride by acid method - HCBBS Forum
- 【HaiChuan Chemical Project Updates】Jiaxing Petrochemical plans to carry out a technical upgrade project to produce 3 million tons of purified terephthalic acid per year - HCBBS Forum
- For environmental inspections of liquid ammonia storage tanks, is it required to have a 200 m³ emergency pool? - HCBBS Forum
- Pressure vessel head - HCBBS Forum
- Regarding the calculation of the outlet diameter of safety valves - HCBBS Forum
- Fire hazard classification of 85% phosphoric acid? - HCBBS Forum
- Regarding the issue of pipeline number boundaries - HCBBS Forum
- Design for converting a methanol tank to store butyl acrylate - HCBBS Forum
- Design of small-hole spray distributor - HCBBS Forum
- Discharge destination at the safety valve outlet - HCBBS Forum
- Should the nominal pressure of chlorine pressure pipelines be 5.0? - HCBBS Forum
- Issues regarding fire separation distances for storage tanks as per detailed regulations - HCBBS Forum
- Seek application technologies for MOF materials in the industrial purification of crude ethylene - HCBBS Forum
- Does connecting the exhaust pipes of storage tanks containing different materials reduce the distance between the tanks? - HCBBS Forum
- How to calculate the air release time for a gas storage tank - HCBBS Forum
- Seeking advice on explosion prevention in offices, shift change rooms, and analysis laboratories within the production areas of petrochemical enterprises - HCBBS Forum
- Letter regarding the clarification of matters related to including the major hazard sources involved in hazardous chemical pilot production construction projects within the scope of supervision - HCBBS Forum
- Requirements related to low-temperature impact for steel used in low-temperature pipelines - HCBBS Forum
- Is the fire hazard of formic acid classified as Class B or Class C? - HCBBS Forum
- Overall location of the cafeteria - HCBBS Forum
- Steam condensate utilization issue - HCBBS Forum
- Issue regarding the origin of the calculation formula for the control valve CV - HCBBS Forum
- Urgently seeking candidates for chemical engineering design, R&D, and electrical instrumentation roles - HCBBS Forum
- I’m seeking advice from experts: what material should be used for pipes carrying ammonia at a low temperature of -30°C? - HCBBS Forum
- Can double-ended studs be used for EO pipe flange connections? - HCBBS Forum
- I need help understanding the purpose of such a design - HCBBS Forum
- Explosion-proof design for the hydrogen peroxide dosing room - HCBBS Forum
- How is the length of the straight sections before and after the flow meter determined? - HCBBS Forum
- Why are the main structural columns in large automated warehouses made of precast concrete columns rather than steel structures? ? ? - HCBBS Forum
- Series of 3D plant design software for chemical projects----AutoPLANT Piping series - HCBBS Forum
- Design schedule - HCBBS Forum
- Seeking advice on burst disc issues with equipment - HCBBS Forum
- Why is loading generally done in an unsealed manner? - HCBBS Forum
- Vacuum problems in vacuum distillation columns - HCBBS Forum
- What is this on the drawing? - HCBBS Forum
- PDMS, SP3D 3D model design - HCBBS Forum