English — Forum #337 (Page 44/163)
- 【Haichuan Equipment Guessing Game】Can you figure out what kind of equipment this is just by looking at the flowchart? Huh? - HCBBS Forum
- Does the emergency pressure relief manhole have an option for connecting external pipes? Collect the discharged gas/liquid - HCBBS Forum
- Old K says every week – talking about things in the petrochemical design industry. Post 50: The handwheel of control valves and valve assemblies - HCBBS Forum
- Repair ABB positioner - HCBBS Forum
- Blockage of the bottom insertion pipe in the reactor - HCBBS Forum
- How is it calculated how much fire-fighting foam is needed for a 30-cubic-meter methanol storage tank? Also, how is the appropriate pipe diameter determined? - HCBBS Forum
- Recycling of flash vapor - HCBBS Forum
- Why is alumina transported pneumatically? - HCBBS Forum
- Looking for a book: BASF citral process - HCBBS Forum
- Issues with grid installation in fixed-bed reactors? - HCBBS Forum
- Calculation of R22 flash volume - HCBBS Forum
- Plate type flat welding flange and necked flat welding flange - HCBBS Forum
- Temperature of ammonia synthesis tower - HCBBS Forum
- High turbine vacuum - HCBBS Forum
- Flow meter installation - HCBBS Forum
- HG20519 is shared with everyone - HCBBS Forum
- Explosion protection rating issues for methanol to formaldehyde conversion - HCBBS Forum
- Are there requirements for a straight pipe section for the installation of the flow restriction orifice plate? Is there a direction or not? - HCBBS Forum
- SA-1000 - HCBBS Forum
- The issue of the composition ratio of benzene, toluene, and xylene in catalytic reforming for aromatic hydrocarbon production - HCBBS Forum
- Treatment of highly toxic exhaust gases - HCBBS Forum
- TCCSAS 007—2020 Implementation Specifications for Change Management in Chemical Enterprises - HCBBS Forum
- The steam pipeline through which steam directly heats the water vibrates violently; can installing an expansion joint solve the noise problem? - HCBBS Forum
- Assessment - HCBBS Forum
- Could you recommend any manufacturers capable of calculating and producing high-quality tower-type equipment such as strippers, ammonia distillation towers, ammonia absorption towers, and stripping towers? - HCBBS Forum
- Seeking expert help: design documents for bromine production via acid method - HCBBS Forum
- Issues regarding using Aspen to simulate the viscosity of high-pressure natural gas - HCBBS Forum
- Which company does a good job with heat recovery? - HCBBS Forum
- What is the current price of steam condensate? - HCBBS Forum
- How is pneumatic valve interlock represented? - HCBBS Forum
- What is the effect of the side-stream yield from a packed distillation column on the temperatures at the top and in the column body? - HCBBS Forum
- Purification of PLA - HCBBS Forum
- Flange drip-proof insulation system - HCBBS Forum
- Regarding French fire protection standards and GB50016, can we choose either one? When checking the fire protection facilities in this factory building, we found many issues that do not comply with the \"GB50016 Code for Fire Protection Design of Buildings\". The design team said it belongs to the installation industry, and factories like ours are related to nuclear power - HCBBS Forum
- I was wondering if any of you have requirements related to organic fluorine chemicals, such as tetrafluoroethylene, hexafluoropropylene, electronic-grade ammonium fluoride, electronic-grade hydrogen fluoride, and so on. - HCBBS Forum
- Hydrogen supply station - HCBBS Forum
- On the design of analytical testing - HCBBS Forum
- Search: Chemical Process Design Manual, 5th Edition, Figure 35-1 - HCBBS Forum
- Hazardous chemical waste is different from hazardous waste, right? - HCBBS Forum
- Maintenance, repair, and overhaul methods for petrochemical York chillers - HCBBS Forum
- Our company produces ethanol gasoline, and we have recently noticed that the top of the ethanol storage tank has turned black. What could be the cause? - HCBBS Forum
- I would like to ask how to deal with esters with high acidity - HCBBS Forum
- Diesel hydrogenation reactor - HCBBS Forum
- Chlorine gas cylinder - HCBBS Forum
- Air flow conversion - HCBBS Forum
- Circle and Square - HCBBS Forum
- I ask all forum members to help find the source of this table - HCBBS Forum
- Xiaobai asks for advice - HCBBS Forum
- What should be included in the operating procedures of chemical enterprises? - HCBBS Forum
- Selection of insulation materials - HCBBS Forum
- Regarding the effect of the reboiler circulation rate on steam consumption - HCBBS Forum
- Discussion on the operating procedure of double-effect distillation (double-effect countercurrent) - HCBBS Forum
- Condensation water appears on the outer walls of the liquid caustic storage tank and the hydrogen peroxide storage tank - HCBBS Forum
- Size of the thermometer port on the glass-lined reactor - HCBBS Forum
- Electrical installation tray - HCBBS Forum
- Issues with the air compressor station, thank you for your answer - HCBBS Forum
- When using a flame arrester with a vent valve, is it integrated as one unit, or are the flame arrester and the vent valve separate components that are assembled together on site? - HCBBS Forum
- Seeking literature - HCBBS Forum
- How to solve it - HCBBS Forum
- Old K says every week -- Post 52: How to consider the exhaust volume of the breathing valve under fire conditions - HCBBS Forum
- What does Class A technical documentation include in engineering construction? - HCBBS Forum
- After the installation of pressure pipelines is completed, in addition to conducting a water pressure test to check for leaks, what other standards are required for inspection and acceptance? - HCBBS Forum
- Calculation of compressed air flow rate - HCBBS Forum
- Why are catalysts B and C mixed together before being added to the reactor in the polypropylene production process? - HCBBS Forum
- Can a safety valve be installed horizontally? - HCBBS Forum
- What material is suitable for use when wastewater contains hydrogen bromide and bromine? - HCBBS Forum
- In a wall-mounted heat exchanger, heat exchange occurs between the two fluids under turbulent conditions. The convective heat transfer coefficients for hot and cold fluids are 150 kW/(m2·℃) and 300 kW/(m2·℃), respectively. - HCBBS Forum
- Adjustments to the centrifuge for anti-surge protection - HCBBS Forum
- How to produce pharmaceutical-grade ferrous sulfate from ferrous sulfate produced as a by-product of titanium dioxide production - HCBBS Forum
- Six types of petrochemical and chemical process equipment are to be phased out by a set deadline, effective from January 1, 2022 - HCBBS Forum
- How should the measured variable H (manual) for instrument functions be understood? - HCBBS Forum
- What is the maximum pressure that stainless steel clamped pipe connections can withstand? Are there any guidelines? - HCBBS Forum
- According to the petrochemical regulations, what are plant storage tanks and groups of plant storage tanks? Must a plant storage tank be just one tank with no more than one, while a group of plant storage tanks must consist of multiple tanks? - HCBBS Forum
- Acetylene issues in the deep cooling section of ethylene plants - HCBBS Forum
- Can a burst disc withstand negative pressure in the equipment, and activate to protect the equipment once a certain level of negative pressure is reached? - HCBBS Forum
- 98.8 meters! The largest equipment for aromatic compounds at Jiujiang Petrochemical has been successfully lifted into place - HCBBS Forum
- How do you bring in and take out the large equipment in the factory building? Enter through the door? From the top of the factory building? - HCBBS Forum
- Recovery of potassium chloride and hydrochloric acid from a mixed solution of potassium chloride, magnesium chloride, and hydrochloric acid - HCBBS Forum
- Production process of magnesium fluosilicate - HCBBS Forum
- How much propylene can a 400-liter and a 1000-liter spherical tank hold respectively? - HCBBS Forum
- Problems in water hammer calculation - HCBBS Forum
- Propylene glycol methyl ether acetate: reactions, acidity issues - HCBBS Forum
- Principles of Chemical Engineering: A fluid with a certain mass flow rate flows turbulently inside a straight pipe with dimensions of φ25mm×2.5mm. . . Help needed - HCBBS Forum
- [Control Systems] Looking for a video tutorial on Honeywell DCS? - HCBBS Forum
- I would like to know how to determine the exhaust air volume in the production workshop; the pipes have a DN500 diameter. What methods can be used to find out the actual exhaust air volume? - HCBBS Forum
- An instrument that emits blue light, for installation purposes – what is it? - HCBBS Forum
- Distance requirements between the substation and storage tanks in an oil depot - HCBBS Forum
- Purification of carbon dioxide gas - HCBBS Forum
- Calculation of expansion pressure in a closed container filled with liquid - HCBBS Forum
- To heat pure water using wastewater at 100°C and make use of the waste heat, what type of heat exchanger scheme should be employed? - HCBBS Forum
- Sodium hydroxide and water simulation - HCBBS Forum
- Project kickoff meeting - HCBBS Forum
- Seek part-time experts to assist the company with inspections: one for the general layout, one for fire emergency preparedness, and one for safety management - HCBBS Forum
- Regarding the issue of pressure boundaries - HCBBS Forum
- Must the inner diameter of the pipes between the serve and receive buckets be the same? - HCBBS Forum
- Steam jet mixer calculation - HCBBS Forum
- Review: Latest Progress on Domestic Ten-Million-Ton-Class Refining and Chemical Projects (Updated Version) - HCBBS Forum
- How should pressure testing be carried out for nitrogen-sealed storage tanks? What standards should be referred to for pressure testing? - HCBBS Forum
- Hydrolysis of carbonyl sulfide to hydrogen sulfide - HCBBS Forum
- Which is better, PLANT 3D or CADworks? What other good 3D software is there? - HCBBS Forum