Refinery-wide Maintenance Vent Compliance Program Development - - PowerPoint PPT Presentation

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Refinery-wide Maintenance Vent Compliance Program Development - - PowerPoint PPT Presentation

Refinery-wide Maintenance Vent Compliance Program Development Strategies Presented by Phil Fish, Barr Engineering Co. pfish@barr.com April 2018 Miscellaneous Process Vent (MPV) and Maintenance Vent (MV) Overview Presentation Group 1


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SLIDE 1

Refinery-wide Maintenance Vent Compliance Program Development Strategies

Presented by Phil Fish, Barr Engineering Co. – pfish@barr.com April 2018

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SLIDE 2

Presentation Overview

  • Miscellaneous Process Vent (MPV) and

Maintenance Vent (MV) Overview

− Group 1 MPV vs. Group 2 MPV vs. MV

  • Three phases of refinery-wide MV compliance

program development

▪ Steering ▪ Mobilizing ▪ Implementing

  • Two equipment screening approaches for

sorting equipment into smaller groups

− Reference-Volume approach − Three-Groups approach

  • Program documentation considerations
  • Ongoing program improvement strategies
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SLIDE 3

MV Regulatory Background

  • MPVs are broadly defined as gas streams

discharged from a process unit

  • Dec. 2015 rule adds work practice

standards (WPS) resulting from removal of the Startup, Shutdown, Malfunction (SSM) exemption

  • Compliance date of August 1, 2017, or

2018 if extension has been granted

  • Prior to compliance date, comply with

general duty to minimize emissions for each maintenance activity

  • EPA technical rule amendments signed on

March 19, 2018

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SLIDE 4

MPV Group Designations

Group 1 MPV

>72 lb VOC/day emissions Route to flare, heater or CE

MV>72

>72 lb VOC inventory Measure LEL (or <5 psi)

Group 2 MPV

<72 lb VOC/day emissions One-time notification

“For vents only used as a result of startup, shutdown, maintenance, or inspection of equipment where equipment is emptied, depressurized, degassed or placed into service”

MV<72

<72 lb VOC inventory Document calculations

MVBlinding

<2 psi (proposed) Document justification

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SLIDE 5

Individual MV Compliance Flow Chart

  • Three basic steps:

1. Determine applicability (before event) 2. Control and monitor emissions for compliance (during event) 3. Complete required recordkeeping and reporting

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SLIDE 6

Phased Compliance Strategy

Steering I

  • What are the interpretations, assumptions and

risks with different compliance approaches?

  • Who is responsible for certain tasks?

Mobilizing II

  • How will each piece of equipment comply?
  • How do we estimate VOC emissions or the mass

contained?

Implementing III

  • How do we manage compliance on a day-to-day

basis for individual equipment maintenance?

  • How do we manage compliance for large unit

TARs?

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SLIDE 7

Steering Phase (1/2)

  • Goal: Determine key interpretations,

assumptions and risks for compliance.

  • Non-linear – may need to revisit initial

decisions based on new/additional information

− EPA rule changes or clarifications − Field measurements − Chemical cleaning vendor guarantees

  • On-board key refinery stakeholders

− Operations, Maintenance, Engineering, Turnaround Planner, Environmental, Safety

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SLIDE 8

Steering Phase (2/2)

  • Evaluate current venting practices

− Can the refinery meet the WPS today? − What are the current procedures when equipment is >10% LEL? − How is equipment vented during planned TAR? − What pyrophoric equipment is connected to a pure hydrogen supply?

  • Align on key regulatory interpretations

− G2 MPV vs. MV − Review EPA’s April 2017 responses to AFPM/API July 2016 request for clarifications.

  • Evaluate practice changes or strategies

− Additional purge cycles − Longer chemical cleaning − Capital projects to better prepare equipment for venting

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SLIDE 9

Mobilizing Phase (1/2)

  • Goal: Collect additional information and

assimilate into spreadsheet(s) to determine how to comply for each vent.

  • Follow the key Steering Team decisions

and interpretations.

  • Smaller team

− Engineering, Environmental, Turnaround Planner

  • Evaluate available process stream data sets

− HYSYS/ASPEN modeling, storage tank representations, etc.

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SLIDE 10

Mobilizing Phase (2/2)

  • Gather inventory of vents (equipment and

piping sections)

  • Develop calculation templates

− Calculate VOC mass in gas and residual liquid from equipment and associated piping

  • Utilize assumptions to screen equipment

into smaller groups

  • Gather empirical data to inform steering

decisions

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SLIDE 11

Mobilizing Phase - Calculation Refinement Hierarchy

Worst-case

  • Saturated temperature
  • Maximum pressure per Safety
  • Process stream speciation

Refinements

  • Steam / nitrogen purging
  • Realistic T&P
  • Equipment measurements

Empirical Data

  • Method 21 screening
  • Method 18 bag sampling
  • Field-measured T&P

Increasing effort Increasing accuracy Increasing sensitivity to changes

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SLIDE 12

Mobilizing Phase - Equipment- Based Screening

  • Screen equipment into smaller groups

− Reference-Volume approach − Three-Groups approach

  • Searching for low-hanging fruit
  • Exclude small equipment unable to contain 72 lb

VOC of vapor

− Worst-case assumptions − Doesn’t account for clingage or liquid heel

  • “Rule of thumb”-type exercise

− Can the equipment contain >X% of 72 lb VOC with worst-case assumptions? − Safety factor to account for uncertainty (clingage)

  • Utilize process engineer’s knowledge/experience

to reduce calculation burden and improve accuracy

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SLIDE 13

Reference- Volume (RV) Screening Approach

>72 lb VOC

  • Towers
  • Reactors
  • Drums
  • Small drums w/ piping
  • Large HX w/ piping
  • Long piping runs

<72 lb VOC

  • HX
  • Pumps
  • Filters

VOC 72 lb

WPS (LEL or, if cannot measure LEL, <5 psi) MV Calculation Documentation (or possibly treat as G2 MPV)

Compliance Demonstration Strategy

Volume RV (X ft3)

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SLIDE 14

Three-Groups Screening Approach

>72 lb VOC

  • Towers
  • Reactors
  • Drums

Approx 72 lb VOC

  • Small drums w/ piping
  • Large HX w/ piping
  • Long piping runs

<72 lb VOC

  • HX
  • Pumps
  • Filters

VOC 72 lb

WPS (LEL or, if cannot measure LEL, <5 psi) MV Calculation Documentation (or possibly designate as G2 MPV) WPS

  • r

MV Calculation Documentation

Compliance Demonstration Strategy

Volume V72 (X ft3)

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SLIDE 15

RV or V72 Process Engineer Questionnaire Workflow

Equipment List RV or V72 Analysis Unit Process Engineer Questionnaire Equipment <<RV or V72 Equipment ~V72±X% Equipment >>RV or V72

Refine

  • r WPS

Done – MV Calculation Documentation Refine

  • r WPS

Three-Groups Approach Only

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SLIDE 16

Implementing Phase

  • Goal: Determine “boots on the ground”

compliance approach.

  • Full stakeholder team

− Operations, Maintenance, Engineering, Turnaround Planner, Environmental, Safety

  • Incorporate WPS into day-to-day
  • perations

− Safe Work Permits − Separate MV documents or inventories listing equipment subject to WPS

  • Establishing procedures for evaluating

venting during upcoming turnarounds

  • Develop recordkeeping procedures
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SLIDE 17

MV Compliance Plan Document

  • Consolidating MV determinations,

calculations and documentation into a single plan

  • Plan main text includes:

− Rule definitions − Steering team decisions and interpretations

  • Appendices include:

− Unit-specific discussion, calculations and process engineer questionnaires − Example recordkeeping forms − Refinery-wide background documentation ▪ RV/V72 calculations

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SLIDE 18

Program Improvement Strategies

  • The goal is to reduce compliance burden
  • r improve accuracy
  • Additional sampling or recordkeeping

− Method 21 screening (concentration) or Method 18 bag sampling (speciation) equipment to validate calculations − Recording T&P data for routine maintenance activities to refine calculations

  • Revising SOPs to improve calculation

parameters

− E.g., do not vent if system pressure is >3 psig.

  • Updating MOC procedures to evaluate

changes to MV applicability

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SLIDE 19

Thank you

Contact information: Phil Fish Barr Engineering Co. (952) 842-3643 pfish@barr.com