English — Forum #337 (Page 29/163)
- In the liquid hydrocarbon decarboxylative desulfurization fixed-bed reactor, the small catalyst particles break apart and expand, pushing aside the wire mesh and grills at the top of the fixed bed and being carried to the back area, where they cause blockages. - HCBBS Forum
- Representation method of SIS interlock - HCBBS Forum
- What are the requirements for the distance between the crane position and the pump? - HCBBS Forum
- Safety technical requirements for oil and gas ventilation at the tops of storage and transportation tank areas in petrochemical enterprises - HCBBS Forum
- Are there any standards specifying the distance between static grounding points for non-metallic pipes and metallic pipes? - HCBBS Forum
- Thiacloprid synthesis catalyst - HCBBS Forum
- On the issue of blast resistance design for buildings [ - HCBBS Forum
- HEDP continuous production process - HCBBS Forum
- Precautions for purchasing used evaporators - HCBBS Forum
- Can a compact structure with the upper layer using circulating water to cool the steam and the lower layer using deep-cold water as the cooling medium be created in the form of a heat exchanger with layers stacked on top of each other? - HCBBS Forum
- Equipment for producing epichlorohydrin by the glycerol method - HCBBS Forum
- The origin of semi-autogenous mills - HCBBS Forum
- Location of the water ring vacuum pump and the condenser - HCBBS Forum
- The feed to the desolventizer tower increases, and the vacuum in the tower decreases - HCBBS Forum
- Fire protection rating of carbon nanotube production facilities - HCBBS Forum
- Regarding differential pressure flow, vortex shedding, mass, and electromagnetic flow – how can the measurement range be expanded? - HCBBS Forum
- Does the temperature of a saturated steam pipeline drop after being depressurized by a pressure reducing valve? - HCBBS Forum
- When competitors engage in price wars within the same market segment, threatening everyone’s ability to survive, what are some ways to break this deadlock? - HCBBS Forum
- Send the appearance of a metering pump; I’m not sure about its working principle - HCBBS Forum
- Dear teachers, what temperature should be set for the outlet temperature of the distillation column feed heater? - HCBBS Forum
- Are there any requirements regarding straight pipe sections before and after the installation of pressure relief valves and safety valves? Are there any other requirements? - HCBBS Forum
- What type of level gauge is suitable for a storage tank with agitation? - HCBBS Forum
- Ningbo Jinfafa 600,000 tons PDH - HCBBS Forum
- Construction organization design for chemical engineering installation - HCBBS Forum
- Engineering documents for atmospheric and vacuum distillation units - HCBBS Forum
- SIL classification and verification - HCBBS Forum
- What to do after the liquid-phase safety valve activates - HCBBS Forum
- Help, I need the names of the substances on both sides of this equation - HCBBS Forum
- The valve model is SD342F1-150R7; could you please tell me what the meaning of these letters is? - HCBBS Forum
- Are the detailed regulations, petrochemical regulations, and construction regulations required to be met simultaneously? If it’s not necessary, which specification should be implemented first? - HCBBS Forum
- May I ask which type of gasoline requires pressurization during transportation and handling? - HCBBS Forum
- How to address excessive fluctuations in the liquid level of the medium-pressure drum - HCBBS Forum
- Classification of pipe base materials - HCBBS Forum
- What should be the set value for the back pressure of the metering pump’s back pressure valve, and what should be the set pressure for the safety valve? - HCBBS Forum
- Aspen12.1 User Manual - HCBBS Forum
- Sodium fluoride, sodium nitrate, 500-1000 ppm, at room temperature, with a alkalinity of 3-4%, can carbon steel be used? - HCBBS Forum
- Issue with bracket numbering in pipeline layout drawings - HCBBS Forum
- According to the standards, under what circumstances is it required to install dual level gauges? - HCBBS Forum
- Questions regarding the selection of material for pipe fittings in gas stations - HCBBS Forum
- Recommendations for the procurement of molten salt for chemical processing plants - HCBBS Forum
- Problems with pump pressure and tower pressure - HCBBS Forum
- The minimum diameter for steel-lined pipes and valves is DN25; however, it is very inconvenient to take samples using DN25. Are there any smaller sampling valves specifically designed for steel-lined systems? - HCBBS Forum
- Can the operating valve be used as an emergency shut-off valve? - HCBBS Forum
- Selection of pump outlet safety valve - HCBBS Forum
- Regarding the issue of inverted exhaust temperature during load adjustment in screw air compressors - HCBBS Forum
- Calculation of liquid chlorine storage tank leakage rate - HCBBS Forum
- Calculation of steam loss during the transportation of steam pipes - HCBBS Forum
- Can the styrene sampling cylinder be online for a long time? - HCBBS Forum
- I heard that desiccants need to be installed at the vent openings of gasoline tanks in gas stations; I’m not sure why. - HCBBS Forum
- Here are the reminders and explanations regarding the key provisions of the \"General Specifications for Industrial Equipment and Pipeline Projects in Plant Areas\" (draft for comments)! - HCBBS Forum
- 【Free Download】Comprehensive Book on Safety Techniques for Hazardous Chemicals – General Volume - HCBBS Forum
- Regarding a benzene concentration of 50,000 mg/m3, is the air diluted before it enters the adsorption system? - HCBBS Forum
- Can the bidder apply for the project approval procedures (planning permits, construction permits, etc.)? - HCBBS Forum
- Acetic acid pyrolysis carbonization - HCBBS Forum
- Help: Corrosion Data and Material Selection Manual - HCBBS Forum
- Seeking advice from experts on thermodynamics problems - HCBBS Forum
- Is there a list of spare parts and wear parts commonly used in engineering, such as pumps, fans, pneumatic valves, instruments, etc.? - HCBBS Forum
- Regarding the issue of whether interlock design should be done in a DCS or SIS system - HCBBS Forum
- What is the appropriate hydrogen-to-nitrogen ratio for ammonia synthesis? What is the appropriate ratio between the amount of syngas and recycled hydrogen? - HCBBS Forum
- Issues regarding the use of liquid ammonia cylinders - HCBBS Forum
- Material addition issue - HCBBS Forum
- Regarding the proportion of flaw detection for pressure pipelines, I would appreciate some guidance from experts - HCBBS Forum
- Are there detailed equipment manufacturing plans, tables outlining key milestones, inspection items, and standards? - HCBBS Forum
- I need a question bank on general knowledge of chemical engineering processes - HCBBS Forum
- Guys, when calculating mass transfer processes with limited mass transfer, how do we determine the gas-liquid mass transfer coefficient? - HCBBS Forum
- How are the auxiliary materials for insulation of equipment and pipelines determined? - HCBBS Forum
- De-fluorination resin - HCBBS Forum
- Is there a more detailed table showing the corrosion resistance of PE, PP, PO, etc.? - HCBBS Forum
- The water pump vibrates heavily - HCBBS Forum
- Which scheme for the gas-liquid separator is more reasonable? - HCBBS Forum
- Chlorine buffer tank - HCBBS Forum
- Stirring tank viscosity sensor - HCBBS Forum
- The issue of the relative density of oxygen - HCBBS Forum
- May I ask if the surface energy of the carbon steel seat can be welded to Stellite? Cladding with Alloy6 - HCBBS Forum
- Calculation of pipeline flaw detection ratio - HCBBS Forum
- Height requirements for the exhaust pipes of the exhaust emission outlets and emergency emission outlets of oil and gas recovery facilities - HCBBS Forum
- What is the difference between these two explosion protection ratings? Is there a big difference in price? - HCBBS Forum
- For waste gas treatment projects handled by environmental protection equipment companies that lack design qualifications, is it possible to produce as-built drawings? - HCBBS Forum
- The water volume is large; should pH adjustment be done online or in a tank? Tanks require too much space and involve high costs - HCBBS Forum
- Who knows the progress of Cangzhou Dahua’s MDI project? - HCBBS Forum
- Should a combustible gas detector or a toxic gas detector be used for methanol? - HCBBS Forum
- Calculation of liquefied gas volume for furnace drying - HCBBS Forum
- What is this? - HCBBS Forum
- May I ask whether a condenser is required for storage tanks of flammable liquids or volatile liquids? - HCBBS Forum
- What type of safety valve should be used for the return inlet of the pump outlet safety valve? - HCBBS Forum
- Amine solution degradation - HCBBS Forum
- Regarding the nitrogen sealing of the solvent storage tank, the reason for the exhaust pressure of 3000 Pa at the single exhaust valve - HCBBS Forum
- Is it safe to use steel-lined plastic storage tanks for methanol and ethanol? Is it allowed by the regulations? How to export static electricity? - HCBBS Forum
- DMF dehydration, what is the role of a packed tower? - HCBBS Forum
- PID flow diagram for hydrogen production via methanol cracking - HCBBS Forum
- CSB Accident Investigation Report Formosa_IL_Report-Chinese - HCBBS Forum
- Ask a simple question: Regarding coke oven gas issues - HCBBS Forum
- Pipeline flow meter - HCBBS Forum
- Is there a valve that can automatically discharge water as soon as it appears in the exhaust gas treatment pipeline? Automatic separation of gases and liquids, similar to a steam trap - HCBBS Forum
- Chemours N324 For sale - HCBBS Forum
- Registered Chemical Engineer Examination - HCBBS Forum
- What is the purpose of connecting a nitrogen supply to the fan? - HCBBS Forum
- How should one go about creating a set of skid-mounted product series similar to those used for activated carbon adsorption? - HCBBS Forum
- Wall thickness of Sch20 - HCBBS Forum
- What is the internal structure of an RTO regenerative incinerator? - HCBBS Forum