General Discussion Forum Introduction
Welcome to the General Discussion forum. This section is for general queries, comments or suggestions that do not clearly belong to the topic-specific forums.
Use this forum when you are unsure whether your post belongs to Improved Practices, New Technologies or Troubleshooting. General comments, forum-related questions and cross-functional technical queries may be posted here.
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Welcome to the General Discussion forum. This section is for general queries, comments or suggestions that do not clearly belong to the topic-specific forums.
The member asks whether it is a good practice to use LP Heater-4 outlet initial flushing line water from another unit for boiler filling during initial cold start-up. The water temperature is around 140°C and the concern is thermal stress or related issues in a 300 MW coal-fired boiler.
Requested more details to understand the operating condition before commenting further.
Additional administrator follow-up is available in the original thread.
A 660 MW unit is procuring flat strips for water wall welding using SA 387 Grade 12 Class 2 material. The supplier has provided a test certificate but not the heat treatment chart. The member asks whether heat treatment can be verified on the finished product by hardness or any other method, and whether IBR hardness limits for one chrome half moly material apply to this grade.
The member raises questions on colloidal silica increase in drum water, why saturated steam silica may remain low despite boiler water silica increase, possible silica slippage in ion exchange systems, and the role of WAC/WBA/SBA/MB sequencing in DM plant operation.
The expert explains the effect of cycle of concentration, the small relative effect of spray flow on main steam silica, the importance of measurement accuracy, silica removal through SBA/MB, regeneration issues and the role of WBA/WAC in reducing ionic load before SBA.
The member asks how a safe boiler water silica limit is determined, whether the limit can be revised based on international guidance, and how much blowdown can ideally be given through CBD/IBD arrangements.
The expert refers to CEGB, EPRI, ABMA and IAPWS guidance, notes the importance of OEM limits and possible carryover concern, and clarifies that CBD should be used as required while IBD should not be used continuously unless sludge removal is needed.
The member seeks conceptual clarity on how suspended and colloidal impurities, though non-reactive, carry surface charges and get attracted to positively charged aluminium hydroxide flocs formed during alum coagulation.
The expert explains the difference between non-reactive colloidal particles and their electrostatic surface charge, the role of zeta potential, colloid stability and how positively charged hydroxides destabilize particles to form removable flocs.
The member reports unsafe violent steaming and truck body heating during wet handling of fly ash from a CFBC boiler, due to excess unreacted CaO reacting with water, and asks how the condition can be avoided when wet handling is compulsory.
The expert suggests reducing unreacted CaO by correcting ineffective lime dosing, using properly sized crushed lime, adjusting SA/PA ratio and refreshing bed material more frequently to improve sulphation effectiveness.