APOLLO AUTOMATIONJAMES WARREN · ENGINEERING & PROJECT LEADERSHIPCASE-071 · Engineering case
Developed an engineering AFE to redesign a failing reduction steam manifold and optimize PRV control before installation funding.
The plant needed engineering analysis before replacement because line size, pressure strategy, PRV selection, and jacket demand had to be validated rather than copied from the failing legacy system.
Steam-Manifold and Pressure-Reduction Engineering
Improved steam-control design readiness and PRV replacement defensibility.
Workstream Portfolio Rollup
16,297,000 USD
Steam and Boiler System Modernization
Recorded workstream portfolio reference. This is the workstream-level value and is not a project expenditure or a new total of reassigned projects.
| Measure | Value | Type & meaning | Attribution & operating context |
|---|---|---|---|
| Initial Jacket Steam Pressure | 20 psi | Design Parameter Pressure-analysis basis | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Initial batch heating — 20 psi for 1-2 hours |
| Initial Heating Period | 1 to 2 hours | Design Parameter Pressure-analysis basis | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization 20 psi initial heating — 20 psi for 1-2 hours |
| Maintenance Jacket Steam Pressure | 8 to 10 psi | Design Parameter Pressure-analysis basis | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Remainder of two-day batch — 8-10 psi for remainder of two-day batch |
| Condensate-Pump Power Range | 1 to 2 HP | Equipment Rating Equipment reference | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization 1-2 HP condensate pumps. |
| Existing PRV Inlet Diameter | 4 in | Baseline Existing condition | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Existing PRV Inlet Diameter |
| Jacket Supply Line Diameter Under Evaluation | 3 in | Design Parameter Design question | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Open steam-system engineering question before installation funding — Jacket supply line diameter under evaluation |
| Pressure Alternative Under Evaluation | > 10 psi | Design Parameter Design question | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Open steam-system engineering question before installation funding — Pressure alternative under evaluation |
| Reported Valve and Pipe Erosion Exposure | 10 year | Baseline Condition history | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Reported Valve and Pipe Erosion Exposure |
| PRV Operating-Pressure Range | 20 to 100 psi | Historical/Reference Value Operating-profile reference | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Steam and condensate study — Operating range considered in the PRV and jacket-supply study. |
| Batch Duration for Steam-Pressure Profile | 2 day | Historical/Reference Value Operating-profile reference | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Steam and condensate study — Batch duration for the initial heating and lower-pressure holding stages. |
| Prior Condensate Return Diameter | 3 in | Baseline Prior equipment condition | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Steam and condensate study — Diameter of the condensate return discussed in prior upgrade lessons. |
| Replacement Condensate Return Diameter | 0.5 to 1 in | Historical/Reference Value Prior upgrade reference | Applies to: Reduction Steam Delivery Manifold Redesign and PRV Optimization Steam and condensate study — Smaller condensate-return sizes considered with 1–2 HP pumps. |
Defined the engineering and repair approach to address pipe erosion, valve wear, high noise, poor low-pressure control, and unsafe manual operation, while reducing the risk of premature installation decisions.
Improved steam-system engineering readiness, measured by evaluation of the 4 in PRV inlet, legacy 3 in steam supply, 20 psi initial jacket steam period, 8-10 psi maintenance period, and two-day batch duty, by developing P&ID, line-sizing, PRV, equipment-specification, and installation-scope deliverables before capital installation.
4 in PRV inlet; 3 in legacy steam supply; 20 psi for 1-2 hours; 8-10 psi for remainder of two-day batch; 1/2in to1 in condensate return lines; 1-2 HP condensate pumps.
Food and Beverage Manufacturer
Owned the full project lifecycle, from capital planning through commissioning and post-startup support. Degraded steam piping and manual throttling created a combined reliability and control problem.
TSK-000190 · Action
Restoring Automated Batch-Temperature Control
TSK-000191 · Action
Restoring Automated Batch-Temperature Control
TSK-000192 · Action
Restoring Automated Batch-Temperature Control
TSK-000193 · Action
Restoring Automated Batch-Temperature Control
TSK-000194 · Action
Restoring Automated Batch-Temperature Control
TSK-000195 · Action
Restoring Automated Batch-Temperature Control
TSK-000196 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000197 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000198 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000199 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000200 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000201 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000202 · Technical scope
Restoring Automated Batch-Temperature Control
TSK-000204 · Action
Restoring Automated Batch-Temperature Control
TSK-000205 · Method
Restoring Automated Batch-Temperature Control
TSK-000207 · Technical context
Restoring Automated Batch-Temperature Control
TSK-000886 · Action
Steam-System Repair and Temperature-Control Retrofit
Recorded application
TSK-000887 · Action
Steam-System Repair and Temperature-Control Retrofit
Recorded applicationTSK-000888 · Action
Steam-System Repair and Temperature-Control Retrofit
Application context. Are steam supply, distribution, condensate and controls coordinated for the operating duty?
Action
Applies capabilities
ACTIVITIES IN CONTEXT
TSK-000154 · Action
Reduction Steam Delivery Manifold Redesign and PRV Optimization
TSK-000155 · Method
Reduction Steam Delivery Manifold Redesign and PRV Optimization
Full lifecycle project ownership
Owned the full project lifecycle: capital planning and prioritization, need definition, feasibility and scope development, engineering and AFE justification, procurement and vendor coordination, construction sequencing and field oversight, commissioning, turnover, and post-startup support. Connected operating requirements with technical scope, funding decisions, execution readiness, and the needs of operations and maintenance.
The steam study describes a 4-inch PRV operating across 20–100 psi, about 20 psi at jackets for 1–2 hours, followed by 8–10 psi through a two-day batch. Noise, valve wear and pipe erosion informed PRV replacement coordination. Prior condensate lessons compared a 3-inch return and mechanical pumps with 0.5–1-inch returns and 1–2 HP pumps.
Objective: obtain engineering AFE funding for P&ID development, line sizing, equipment specifications, and installation scope, and assess PRV replacement to reduce noise and improve efficiency.
Existing condition: a 4-inch PRV inlet serving tank steam jackets, condensate return, and pressure-control challenges.
High-priority redesign questions: whether a 3-inch supply is needed to both tank jackets, whether pressure above 10 psi could reduce piping and eliminate a second PRV, and what materials would mitigate wear/erosion.
PRV issues stated: noise, significant valve and pipe erosion over 10 years, and difficulty with precise low-pressure control.
Options: retain a 3-inch line with PRV or downsize to actual demand; evaluate new or remanufactured PRV.
Deliverables: P&ID, engineering report, specification list, installation SOW, and estimate.
Next steps: engineering AFE, engage controls integrator, finalize P&ID/specifications, and raise a separate installation AFE.
Owned the full project lifecycle: capital planning and prioritization, need definition, feasibility and scope development, engineering and AFE justification, procurement and vendor coordination, construction sequencing and field oversight, commissioning, turnover, and post-startup support. Connected operating requirements with technical scope, funding decisions, execution readiness, and the needs of operations and maintenance.
Investigated retrofit alternatives and coordinated piping repair, insulation, control valves, RTDs and commissioning. Restoring automated temperature control linked mechanical integrity with process safety and consistent operation, replacing the need to manage temperature through manual steam throttling.
