English — Forum #336 (Page 21/51)
- Technical summary: Are there 4 holes or 8 holes for the flange bolt holes on DN65 valves? - HCBBS Forum
- Fire water volume design for LNG liquefaction plants - HCBBS Forum
- Is the outlet of the storage tank’s breather valve connected to an environmental protection gas collection hood or directly via a flange? - HCBBS Forum
- Installation of gas and liquid transfer pipes - HCBBS Forum
- What does “smoldering” mean in the list of key flammable dusts in the industry and trade sector? - HCBBS Forum
- How can open-type equipment achieve nitrogen sealing? For example, in the case of equipment with a circular opening, is it possible to create a gas curtain by installing nitrogen nozzles at the top in order to achieve nitrogen sealing? - HCBBS Forum
- Is a fixed location required for the storage design of Class C warehouse materials? - HCBBS Forum
- Pipeline number interpretation - HCBBS Forum
- What does a pipeline layout plan mean? - HCBBS Forum
- Where do the higher and lower pressures of the two safety valves on the ammonia tank come from? - HCBBS Forum
- Recovery of dichloromethane vapors and emission within specified limits - HCBBS Forum
- What is the purpose of the detection riser installed in a single-layer methanol tank buried in a tank pit? - HCBBS Forum
- Electronic Book: “Pipeline Stress Analysis and Engineering Applications” - HCBBS Forum
- Coal types for gasification - HCBBS Forum
- What is the melting point of 68% nitric acid? - HCBBS Forum
- Chemical piping software - HCBBS Forum
- Issues with the layout of laboratory facilities throughout the plant - HCBBS Forum
- Toluene is used as a water-carrying agent. How to use a density meter with a shut-off valve to automatically separate water and allow toluene to flow back to the reactor? - HCBBS Forum
- Free tutorial on how to use the flare gas separation tank calculation sheet - HCBBS Forum
- How should the centrifugal mother liquor from a triple-effect evaporator be treated? - HCBBS Forum
- Some standard covers have a “hydrocarbon” label attached to them – what is the special meaning of this? - HCBBS Forum
- How is the design margin for plate heat exchangers defined? Is it a margin for area, or a margin for the heat transfer coefficient? - HCBBS Forum
- Jacket design and operating pressure - HCBBS Forum
- Can workstations for personnel to perform operations be installed within the framework of a chemical processing plant? Is it considered a structure or a building? - HCBBS Forum
- Guide to Using the Calculation Table for Kv/Cv Values of Control Valves under Installation Conditions (Gases, Steam) - HCBBS Forum
- Explanation on how to use the hydraulic calculation table for packed towers - HCBBS Forum
- Standard SW-2.4 of the ASME B16.20 gasket standard for American standards specifies that centering rings are included; how should concave-convex flanges be used? - HCBBS Forum
- Adipic acid centrifuge and thickener discharger - HCBBS Forum
- Does Haichuan not have a storage and transportation division? - HCBBS Forum
- DL/T5434-2021 Code for Supervision of Electric Power Construction Projects - HCBBS Forum
- Why is an interlock cut-off valve installed at the inlet of the vacuum pump? - HCBBS Forum
- 【SeaChannel Safety Discussion】The design engineer for ladder A048 should climb it himself - HCBBS Forum
- Does the flow rate change after the pressure before and after the pressure relief valve changes? - HCBBS Forum
- Simple oil-water separation, correction of conductivity stratification control drawings - HCBBS Forum
- Do you know? What is project micro-location? - HCBBS Forum
- Welded joint heat treatment - HCBBS Forum
- Requirements for the layout of dust collectors in production workshops - HCBBS Forum
- 【Haichuan Equipment Guessing Game】What is the pyramid made for? ? - HCBBS Forum
- I’m looking for a flow meter that can be used to monitor ammonia levels - HCBBS Forum
- 45° slope of the storage tank insertion tube - HCBBS Forum
- Flow velocity of the fluid in the pipeline - HCBBS Forum
- Evaporation latent heat of liquid ammonia - HCBBS Forum
- Layout of above-ground pipelines? - HCBBS Forum
- Selection of sampling hole format - HCBBS Forum
- Explanation of the calculation sheet for MVR evaporation process in aqueous solutions - HCBBS Forum
- Dear Sichuan friends, Happy Mid-Autumn Festival! - HCBBS Forum
- 【Principles of Chemical Process Safety Design】Valves - HCBBS Forum
- Standards and specifications for engineering design in automation control fields - HCBBS Forum
- High-performance anti-corrosion powder coating - HCBBS Forum
- What are the pressures before and after the natural gas enters the customer’s pressure regulation and metering cabinet outside the plant? General situation - HCBBS Forum
- Design of graphite quench tower - HCBBS Forum
- 【Haichuan Equipment Guessing Game】Are experts planning to rebuild the Western Xia royal tombs? - HCBBS Forum
- The fourth phase of Inner Mongolia Yuanhong Fine Chemicals Co., Ltd., with an annual production capacity of 2,000 tons of DPA, has officially started trial operations - HCBBS Forum
- Can an office be set up in the power distribution room? - HCBBS Forum
- CNPC CPECC North China Branch - HCBBS Forum
- Is it necessary to install a buffer tank at the outlet of the reciprocating vacuum pump? - HCBBS Forum
- Issues regarding the definition of the upstream and downstream boundaries for nitration, chlorination, fluorination, diazotization, and peroxidation processes - HCBBS Forum
- Can Class A installations be installed in the space beneath the chemical pipeline corridor? (e.g., gas pressure regulating cabinets) - HCBBS Forum
- Imports and exports of refined oil loading and unloading stations - HCBBS Forum
- Interval distance for setting rupture discs on long-distance pipelines - HCBBS Forum
- The most comprehensive schematic diagrams of coal chemical processes - HCBBS Forum
- I would like to ask the experts: Are the drawings used for the safety design section and the occupational disease prevention facilities design section in chemical enterprises the same? - HCBBS Forum
- Does LNG cryogenic submersible pump need to be explosion-proof? - HCBBS Forum
- Enthalpy of formation and enthalpy of solution of magnesium sulfate - HCBBS Forum
- SEI wins the EPC contract for a 1.65 million-ton ethylene plant project in the fine chemicals and raw materials sector, worth 5.06 billion yuan - HCBBS Forum
- The total investment for the Zhoushan Jintang New Materials project is estimated to be 67.5 billion yuan - HCBBS Forum
- On the toxicity of benzene-containing exhaust gases and venting issues - HCBBS Forum
- A conical-shaped tank filled with brine; I want to add a stirrer - HCBBS Forum
- Calculation of safety valve discharge capacity under heat exchanger tube rupture conditions - HCBBS Forum
- Discharge of rainwater from chemical plant areas into the sea - HCBBS Forum
- Process package document for the combined production of butene from propylene and formaldehyde - HCBBS Forum
- What material is generally used for pressure components in acetic acid pressure vessels? - HCBBS Forum
- Questions regarding GB50160-2018 - HCBBS Forum
- Control scheme for the superheated water closed-loop system in the reaction kettle - HCBBS Forum
- Regarding the various changes that occur during the project construction process, as well as the approval and evaluation procedures involved - HCBBS Forum
- Is a substitute material needed for the dual-standard material? - HCBBS Forum
- Classification of explosion hazard zones in semi-enclosed areas - HCBBS Forum
- Free tutorial on how to use the calculation table for pipeline pressure drop in vapor-liquid/liquid-solid two-phase flow - HCBBS Forum
- 【Ten Years of Rapid Development in Chemical Equipment】1953–2024: Signing of the design contract for the world’s largest vinyl acetate production facility with an annual capacity of 330,000 tons - HCBBS Forum
- 3D factory design software series for chemical projects----PDSoft series - HCBBS Forum
- Heating and vaporization of aqueous crude oil - HCBBS Forum
- Thermometer installation location - HCBBS Forum
- Computer-based exam for pressure pipeline designers - HCBBS Forum
- Water hammer in steam condensate pipeline - HCBBS Forum
- Stored in a chemical warehouse, different substances that can be stored together without any incompatibilities between them – can they be stacked on top of each other in the same stack? - HCBBS Forum
- Sulfur recovery process - HCBBS Forum
- Several process packages for lubricant hydrogenation, ethylamine, maleic anhydride, succinic anhydride, and PBS - HCBBS Forum
- Chemical project 3D factory design software series----PDMS/E3D series - HCBBS Forum
- Free tutorial on how to use the Excel template for creating progress plans - HCBBS Forum
- Multi-stage control automatic control scheme for reactor temperature - HCBBS Forum
- The discharge capacity issue of steam pipeline safety valves - HCBBS Forum
- Regarding the material used for the external insulation of liquefied hydrocarbon equipment - HCBBS Forum
- How to interpret the General Code for Building Fire Protection GB55037-2022? - HCBBS Forum
- If the volume of the tank area exceeds the fire protection standards specified in the engineering design guidelines for fine chemical enterprises, does that mean these guidelines apply?” - HCBBS Forum
- Why is the storage of potassium permanganate classified as Category A, while potassium permanganate production facilities are classified as Category B? ? ? - HCBBS Forum
- Free explanation of the process calculation sheet for centrifugal compressors - HCBBS Forum
- Natural gas flow rate - HCBBS Forum
- Discussion on sampling locations for exhaust stacks - HCBBS Forum
- Heat exchanger courseware - HCBBS Forum
- Do all chemical process pipelines have to be designed by a design institute? - HCBBS Forum