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Pingxiang Daier Separation TechSep 21, 20264 min read

How to Decide Between Partial and Complete Packing Replacement During a Shutdown

Choosing between partial and complete packing replacement should consider damage distribution, packing age, remaining life, process changes, cleaning quality, compatibility, future shutdown cost, and required operating interval. The best decision minimizes total operational risk, not only immediate material cost.
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Pingxiang Daier Separation TechSep 21, 20263 min read

How to Add an Intermediate Liquid Redistributor to an Existing Packed Tower

Adding an intermediate liquid redistributor can improve performance in tall existing packed towers when liquid maldistribution develops with bed depth. Retrofit design must consider vertical space, collector capacity, pressure drop, support structure, fouling, sectional installation, and remaining packing height.
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Pingxiang Daier Separation TechSep 21, 20263 min read

How to Retrofit a Packed Tower That Suffers from Repeated Fouling and Plugging

Repeated packing fouling should be treated as a system problem involving deposit mechanism, packing geometry, liquid distribution, support design, operating conditions, and maintenance access. A fouling-focused retrofit aims to extend reliable operating time rather than simply replacing contaminated packing.
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Pingxiang Daier Separation TechSep 21, 20263 min read

How to Reduce Pressure Drop in an Existing Vacuum Packed Column

Reducing pressure drop in an existing vacuum packed column requires evaluating packing, support plates, distributors, redistributors, mist eliminators, fouling, and bed height as one pressure-loss system. The retrofit should reduce total resistance while maintaining the required separation performance.
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Pingxiang Daier Separation TechSep 21, 20263 min read

How to Retrofit a Packed Tower When the Feed Composition Has Changed

When feed composition changes, packed tower retrofit should be based on the new mass-transfer duty, hydraulic loads, material compatibility, fouling tendency, liquid distribution, and operating range. Existing equipment should be reassessed against the new process rather than the original design basis.