Showing posts with label 5. Plant Maintenance. Show all posts
Showing posts with label 5. Plant Maintenance. Show all posts

Friday, December 2, 2016

5.5 Plant Maintenance: Refractory Repair

Refractory Repairs




Refractory are similar to lining and coatings, for which the purpose is to protect the metal enclosure from the effects of heat and chemicals.

Refractories are found in fired spaces such as ovens, boilers and reactors

What operators fear during operations is hot gas pass due to refractory failure, this can potentially heat up the metal surface beyond its design temperature reducing the stresses of material. What do I meant by this statement?

Metal properties, in reference to ASME II-D Material Properties, it can be observed from the several charts for ferrous steels that the Maximum Allowable Stress values remain uniform up to approximately 600F before it begins losing it, therefore the ability of the equipment to hold pressure & stress reduces. This issue is especially important for reactors as they normally operate at higher pressures as compared to ovens and boilers.


As a result of the overheating of metal, we not only have a problem holding the pressure, but we also face many other problems if refractory damage is allowed to be left in place. To summarize the ill effects:
    • Exposure of metal surface to harsh process media
      • Exposure to acidic components such as H2S, polythionic acid, naphenthenic acid, ammonia bisulfide, chlorides, hydrogen and many more can result in significant increase in corrosion rates or Stress Corrosion Cracking.
    • Damage to insulating bricks
      • Refractories are normally lined in several layers especially for high temperature service involving harsh chemicals ie. reactors. The penetration of gas through fire bricks can lead to insulating bricks failure.
    • Hot spots
      • Overheating of metal results in red hot spots and eventually metal damage due to creep which causes material to loss its strength over time.


General Acronyms 

  • Hot face bricks - High alumina content to resist high temperatures
  • Insulating bricks/castables - These are usually lined between the hot face bricks and metal wall.
  • Mortar - Adhesive to join bricks, don't use them as castable, they are meant to be thinly spread.
  • Pour castable - Similar to refractory bricks, however for difficult to lay areas to reduce work time. 
  • Ramming Castable - Also known as plastic castable, used for filling voids in castable and refractory brick spaces by injection.



Damage Evaluation and monitoring
Monitoring:
Basic monitoring for refractory condition can be made by online condition assessment from exterior by utilising the following methods to have a glimpse of the metal condition which can reveal whether if refractory have deteriorated.

  • Live Infrared thermography 
    • Monitors hot spots, loss of refractory material by localized or overall temperature increases.
  • Sectional insulation removal 
    • Inspect for distortion and change in OD which are signs of creep, 
    • Inspect for surface glazing which are signs of hot spots

Damage Evaluation
After shutdown of unit, thorough inspection of the equipment can be performed to identify suspected damaged observed during monitoring.

Even if no damage are suspected, brief inspection of the below can also be carried out to identify minor indications especially if operating temperature is much much higher above ambient, as thermal expansion can cause unexpected damage from minor cracks and nicks. Inspect if you can, this is likely your one and only chance in a long time, as plant equipment are expected to be running 24/7 and have high availability!


  • Loss of mortar material or strength
    • Loss of mortar strength between bricks can be caused by improper mixture and application during brick laying.  The physical condition can only be identified offline, tell tale signs are loose bricks, broken castable or cracked refractory. Therefore important properties to watch during repairs and construction are: 
      • Crush strength - Resist compression
      • Adhesion strength - Resist loss of bonding
      • Water content - Gives mason more time for application
      • Air content - More air, more porosity, but good mortar closes up this issue.
      • Time after mixture - Mortar is an adhesive, it loses adhesiveness in air over time.
      •  Quality of brick - Good bricks should have slightly rough surface to improve adhesion with mortar, they should also have low porosity and high crush strength
    • Erosion of refractory or mortar material 
      • In high flow rate furnaces such as gas reactors or those containing 2 phase flow, there will be loss of refractory material. 
      • Mortar having less crush strength than bricks is much easily eroded or damaged by thermal expansion. Watch out for loss of mortar which can increase build up of material between bricks and over time even penetration to insulating layer behind the bricks.
    • Build up of carbon
      • Observed this in a gasifier, which is an incomplete combustion furnace with a feedstock containing high metal content.
      • One of the main product carbon monoxide breaks down into carbon under high temperature with metal as the catalyst with the refractory material acting as an catalyst.
      • Along with erosion of mortar, the carbon built up had penetrated into the area between the bricks and insulating castable as a result pushed the bricks inwards into the furnace and caused several cracks and rise in metal temperature.

  • Crack on bricks
    • Inspect for damaged bricks in suspected areas. 
      • Refractory may contain layers of bricks, should suspected area shows perfection on the hot face, but shows a hot spot on the thermography, hot leak could come from another location within close proximity. 
      • Avoid denial of defects due to good hot face condition, it could be underlying.  
    • Quality of bricks
      • Always ensure quality source or experience with the process. This is beyond quality documents, as documents are usually doctored these days.
      • Perform factory visits, request for sample fabrication and witnessed testing before purchase in placed.
      • Example of tests 
        • Crush strength
        • Porosity (Cutting it up)
        • Rung test (Not effective)

  • Areas with gaps exposing metal surface
    • Inspect metal surface for
      • Corrosion - This contagious issue could spread beyond and behind the refractory
      • Glazing - This is signs of hotspot formation and may cause catastrophic failures.

Repairs and Installation
  • General Information for Refractory Repair
    • Only damaged section needs to be repaired, there is no need to spend excessively
    • For custom shape bricks that do not fit, they can be cut by the mason to fit, but in no case cut it down to less than 1/2 of original size.
    • MDB will state maximum mortar thickness, avoid large joints to minimise failures.
    • For Pour castable refractory, watch out for its preparation process, as there are also factors to monitor such as mixing temperature, mixing time, water content material still within shelf life. 
    • Fill all gaps possible with plastic castable.
    • A frame or form work is normally used for laying bricks/casting on difficult positions such as overhead domes. 

  • Loss of mortar material or strength
    • For such failures, the reasons and what to look out for has been listed above. For the repair be prepared to inspect quality of raw material, quality of workmanship which includes mortar preparation to brick laying process. 
    • Use quality manuals from Manufacturer Data Book or use a Specialist. Workmanship is very important for performance.

  • Crack on bricks
    • For such failures, it usually points to quality of bricks from factory and has been listed above.

  • Areas with gaps exposing metal surface
    • Consult the inspector, repair organization & specialist for repair procedures as it varies from case to case basis. Refer to Pressure Vessel repair section.



Saturday, September 24, 2016

5.3 Plant Maintenance: MOM Statutory Inspections (Singapore)

This post will cover only maintenance aspects of MOM Statutory inspections but not design and construction.

A little story about MOM and its jurisdiction control
MOM is the Ministry of Manpower in Singapore. Under this ministry, a Workplace Safety and Health department takes care of all industrial health, safety, environment related issues.

Pressure vessels, boilers, steam related equipment and more all fall under jurisdiction control. They pay attention to equipment carrying steam, air and refrigerant. Nothing else.

The lack of jurisdiction over equipment carrying other hazardous fluids probably because those are usually taken care of by ASME or CE inspections where most equipment makers needs to comply to.

We also know that steam, air and refrigerant is the most common utilities fluid used in industrial installations since the era of industrialization in 1900s. The rule book was passed down from British Law and developed then on, and little probably changed.


Inspection Intervals
These vessels are required to be inspected during fabrication by an accredited Authorized Examiner(AE) This is similar to the Authorized Inspector(AI) in ASME context. What needs to be done here will not be explained here, as we are more focused on maintenance and operations.

How about during Operations? What requires inspection on an interval basis by an AE.

  • Air/Steam Receivers (PV & exchangers)
  • Piping
  • Steam equipment
  • Safety valves connected to the above devices

Interval and details of inspection
Steam Boilers fired and unfired - 1 year
Steam/Air receivers - 2 year
Refrigerant receivers - During Fabrication and After Repairs
Piping - During Fabrication and After Repairs (For MP and HP steam systems)
Hydrotesting - After repairs or every 10 year
Thickness Measurement - 10 year
Safety valves - Calibrated during the inspection interval

Corporate Level Assessment
New initiatives: Corporate Level Assessment. What is it?
With this intitiative, delayed Statutory inspection intervals could be applied by plant owner. However this is subjected to approval after submission of the relevant maintenance procedures, inspection data and reports, audit reports and etc,

This initiative is designed to be somewhat ambiguous this is so that approval can be made on a case by case basis. However rest assured safety related corruption cases will be weeded out due to high level of interviews on MOM Authorized Examiners and corporations during the submissions.

Under this initiative boilers can be granted extension of 2 years and pressure vessels 5 years. Depending on condition of equipment and documentation submitted. Requiremets are as such
- Competent Person (CP) to be engaged to scrutinize the CLA reports to be submitted ( this is on top of AE and cannot be the same person)
- Yearly Internal Audit to ensure that the below are in place to be done internally. 
- 2 Yearly Audit by an External Agency. (Similar to the internal audit, except that its called a Technical Audit. Requirements for the audit is a long list of reports, as you can see below)
- All related Visual Inspections and NDT shall be carried out by an SAC accredited Inspection Body(IB)
- All related Calibrations shall be carried out by an SAC accredited laboratory
- Scheme For Guaranteed Safe Use (SGSU) to be developed, this is basically the equipment inspection plan, company safety procedure, plant process description, brief maintenance and operation history of equipment to be captured, equipment datasheets & drawings, organization chart of key parties, 
- Produce to auditors yearly eqpt remaining life calc, BFW pump condition monitoring logs, BFW treatment logs, steam blowdown logs, PSV test summary and certs, documents pertaining to RBI if any, past CLA audit reports if any, past CP report if any.
- The above requirement may vary, depending on what is found in the approved SGSU submitted and approved. So do submit only what is within your means and resources. Just follow the SGSU and you will be fine, if not you may be fined or removed from CLA Scheme!

Repairs
All Repairs needs to be informed by writing/emailing to MOM directly for approval by commissioner before appointing an AE for the endorsement of repair. 
Method statement of fabrication, inspection and testing plans will need to be submitted for endorsement by AE and review by MOM. Repair requirements per API 510, NBIC or PCC-2 has so far been accepted, mostly subjective to decision of the AE. 

Tuesday, April 26, 2016

5.4 Plant Maintenance: Valve Repair

Valve Repair

Repair of valve is a pretty straightforward activity to perform.
Valve repairs are very common especially on systems handling steam and corrosive fluids. Beware of steam cuts, it can grow from a condensate droplets to a huge mist cloud in few days. The longer a leak is withheld without repair, the higher the maintenance activity.



1. Various forms of valves problem:
a) Leaking packing gland
Major cause for this problem is corrosion, aging and steam. (Top & Bottom Left Photo)

b) Leaking flange
Major causes of this problem is corrosion, aging, steam, misalignmemt and unsuitable gasket.

c) Leaking bonnet
Major cause of this problem is same as leaking flange, as this item is a flange! (Top & Bottom Right Photo)

d) Passing
Major cause of this problem is unsuitable trim design, aging, improper usage caused by operators with a torque wrench.

e) Knocking and vibration
Major cause of this problem is a
* Design flaw, most likely a stop valve with check valve function is installed and flow rate is at natural frequency of the system.  Or..
* Unsuitable valve for draining/venting/gage installednear a reciprocating equipment which operates at its natural frequency.
Contractor design manual usually covers this, where to locate the drain/vent valves for which size and pipe thickness. Fatigue cracking will come after those who do not review designers work!

f) Corrosion
Major cause of this.. Process spills nearby, leaking flanges, leaking fitting on valve body, located near the sea or a corrosive area. (Top & Bottom Right Photo)


2. And now how to repair ? 

a) Packing gland leak


1) First thing to do will always be to tighten it, however there is always a limit to tightening, eventually there will be no packing left. Sometimes the packing tight bolts are jammed or corroded, so If all fails.. Isolate the line, put in PTW and the usual stuff.

Chesterton 1600 Series Packing Yarn (2016)
Source: Chesterton 1600 Valve Packing Webpage


2) Remove packing with a gland extractor, Replace the gland with original spares or typical repair "yarn" available in most gland material. Use compatible material ie. Teflon for corrosive or cryogenic lines, use graphite with inconel braiding type for hot systems.
* Note that some valves especially pressure seal valves uses a special sandwich packing system comprising of graphite yarn + pure graphite configuration for improved sealing and operatibility.

3) Another way to repair a valve with leaking gland is to tap a hole on the bonnet and inject a sealant. The sealant usually lasts between 2 to 5 years. A more expensive option compared to packing change, if you cant stop the system and leaking fluid from the gland is a huge serious issue in your plant.

4) Some valves have different type of sealing ie. Belleville spring, pressure seal. Refer to IOM for proper repair procedures, original spares are usually recommended for repairing such valves.
I observed a shoddy pressure seal valve repair by lapping the steam cut area and boxup. This clearly doesn't work. Do it good, do it right.

5) If it still keeps leaking upgrade the packing to Chesterton Valve Sealing System 5800 and equivalent. This system basically upgrades your packing to the sandwich type mentioned above and adds live loading spring washers to packing bolts for thermal stress compensation. See picture.
Chesterton 5800 Series Packing Kit (2016)
Source: Chesterton Valve Packing Repair Kit Webpage


b) Leaking flange
1) Same as above, first remedy is usually to tighten. But wait.. Is the bolt head already corroded and rounded? Is the flange still leaking despite tightening, If yes..

2) Isolate the line and break the flange. Inspect the flange and gaskets.

3) Is it a gasket problem ie. Wrong size, material type? Pls install the right gasket!

4) Is it a flange problem? Wrong rating, corroded flange face.

4.1) Corroded flange face can be machined down with onsite machining to achieve required finishing to B16.5 about 250um rms. However do check thickness of flange to ensure u have suffice material.

4.2) What if you cant machine? Use gasket sealant paste, these usually works well if you use good brand like Permatex form A.  Not endorsing any brands here but this is what we have.

4.3) Rarely I face the problem of a incorrectly rated flange. But it is still a possibility. Check the design, operating pressure/temperature vs the flanges. Corrosion of flange face and gaskets are more of a harassing issue which leads to leaking flanges.


c) Leaking bonnet
Refer to leaking flange.

d) Passing
1)Simple.. Change the valve

2) what if its welded or your on a budget constraint ?
a) inspect it and if its in trouble
b) perform a weld build up repair
c) change out the entire trim/bonnet assembly.
These usually fixes the problem, however if they keep returning let say every year, you know there is a problem with the trim material, valve brand or even body design. I have seen some design which promotes crevice corrosion and some design which fails so frequently but others that hold up so well. Do accept a brand change sometimes, its good.

e) Knocking/Vibration
Unfortunately there is no quick fix to this. Redesign the pipe connections or system

d) Corrosion
- Brush it and paint it

- If it keeps pestering you, the material is likely unsuitable, talk to management for an upgrade, usually they would prefer if you brush and paint it though it keeps you busy and may cost more in the long run.

- For the equipment near process spills, my plant had successfully protected them by building mini shelters over where corrosive fluids tends to attack valves, control valves, junction boxes. We build them with insulation cladding, they are extremely cost effective.

- Some valves comes with relief vent ports or hinge pins providing an escape way for process fluid, do expect them to leak overtime and suggest to perform Corrosion Under Insulation checks by creating a window on the insulation at where these points locate, and of course not forgetting to create the Inspection schedule.

Monday, June 1, 2015

5.2 Plant maintenance: Pressure Vessel Repair

Operation stage
  • Operator: Ensure these vessels operates within their specified design limits and measures shall be taken to ensure no overpressure beyond the specified allowable times. Not more than 500h/yr for 20% overpressure and not more than 100h/yr for 33% overpressure. 
  • Mechanical Integrity: Ensure these vessels are constantly monitored on-stream visually, check all vessel body paint, nozzles, stud bolts, supports and anchors are in good condition without distortion or corrosion, inspect under insulation if any suspected damage to insulation are observed and apply suitable non-destructive testing over time time of operation to observe any signs of material failure, especially in processes susceptible to such failure modes. Read API 570 for the recommended inspection intervals and API 571 damage mechanisms for some examples of damages with photos. 


Repair stage
  • What constitutes to a Repair? 
A method to restore the equipment condition to where it can operate safely within the Maximum Allowable Operating Pressure (MAWP) and Allowable operating temperatures.

Adding of nozzles can also constitute to a repair, if
- It does not require a reinforcement pad
- It is smaller than any existing nozzles on the vessel

Adding of any other nozzles are termed an "Alteration", which usually comes with rerating as the vessel strength could be significantly reduced.


  • Avoiding Repairs 
First thing when problems are identified, management point of view may be safety, cost, operational we don't know. But these are all the potential problems to avoid a repair, can we actually avoid?
The answer is yes, and how do we do it?

    •  Rerating
      • Rerating to a lower MAWP and operating pressure for thinned vessel walls for continued operations until minimum thickness is hit again. This is usually the easiest way out.
      • Rerating shall be performed by an Engineer or Manufacturer.
    • Fit For Service Assessments (FFS)
      • In reference to API 510, Chapter 7, it shows how to assess the pressure vessel in damaged condition to extend its life. Not all scenarios are covered, they cover only the usual problems for example pitting, localized wall thinning and wall thinning near by a weld seam.
      • If the problem cannot be found in API 510 Chapter 7, move on to API 579-1 or ASME FFS-1 for the full assessment. They come in level 1 to 3, for 1 is simplest and 3 is detailed. 
      • Level 1 are usually performed by End User Engineers, and level 2 and 3 usually outsourced to software or consultants. 

Nevertheless, basic Risk Assessments should at least be carried out to evaluate the Consequence or Probability of a leak before putting the damaged equipment back to service.

      • Is it hazardous to working persons?
      • Is it environmentally harmful ?
      • Would it affect operations and customers adversely? 


  • When are Repairs required?

The number one reason for a repair would be corrective maintenance. This is usually carried out as follows:

    • [Unplanned] As leakage or damage has been initiated.  
    • [Unplanned] Thinning beyond acceptable thickness, damage is unsafe for continued operation, rerating is not possible and FFS assessment fails,
    • [Planned] Equipment suffers from damages which can last till the next outage 

  • Repairs in USA and Repairs elsewhere
National Board U-stamp vessels: In the USA, the repair shall be performed by a certified NB R-Stamp repair shop under approval of Authorized Inspector in compliance to NB-23.
    • If outside of USA, check local jurisdiction or company best practice for R stamp requirements. If required is usually for Quality Assurance or Company requirements 
    • Generally pressure vessel repairs without R stamp are commonly done. Alternative codes and guidelines can also be used for repairs such as ASME PCC-2 or API 510. Check Company guidelines, if none to consult a pressure vessel engineer.

  • API 510 Inspection, Repair, Rerating & Alterations: 
    • Alternatively an API 510 repair procedure can be used also under the approval of the Authorized Inspector. Refer to Appendix D of API 510 document for the check list
  • Typical repairs based on API 510 includes Temporary and Permanent Repairs.
    • Ensure that all minor repairs are authorized by the pressure vessel inspector before commencement. Approval for major repair may not be given for an ASME Section VIII designed vessel until approved by an experienced Pressure Vessel Engineer.
    • Crack repairs shall be consulted with the pressure vessel engineer before proceeding, as cracks may propagate even after the repair. 
    • Pressure tests may not be required after the repair. Unless it is believed to be necessary by the inspector. Pressure test if required, may be waived if suitable Volumetric NDE are in place to ensure integrity of the repair.
    • Temporary Repairs includes:
      • Lap patch - This is also commonly known as doubler, sometimes could be done on-stream as emergency repairs, if the process fluid is not hazardous or flammable, and welding process permits so.  A plate of usually similar material, properties and profile is welded to the external wall of the pressure vessel over the leaking spot. There are size/thickness restrictions where you need to calculate and avoid welding over to or near existing weld seams, the edges needs to be rounded to minimum 1" radius.



      • Pipe Cap/Nozzle - Welding a pipe cap or nozzle to seal in the leaking spot. These are non-penetrating.

      • Leak sealing - Possible for very small pressure vessels, usually below 8" diameter. The leaking spot could be box in or wrap sealed by epoxy-metal binders.
      • Lap band repair - A huge band is attached around the vessel body, this is not recommended unless the repair needs to remain in place for a longer period of time.


    • Permanent repairs includes:
      • Shell course replacement - cutting out the damaged section for replacement. This is usually an expensive job, especially if done on sections of a huge vertical column, high costs largely attributed to lifting and manpower.

      • Strip lining - a thin layer of sheet metal, usually of a superior material is lined internally. Cheaper than the other methods.


      • Insert Plate - A piece of the pressure vessel is cut out and replaced with a new piece of metal plate of the same profile over the spot of leakage. The edges should always be grounded unless the side falls on an existing weld seam. In contrary to the sketch, the corners of the insert plates shall be rounded to eliminate residual stresses.

      • Weld overlay - Adding a layer of weld filler metal over the thinned down sections of the vessel to restore the wall thickness. Very tedious and time consuming. Watch the manhours.  Take note that the repair thickness shall not be more than 50% of the minimum required thickness of the vessel (exclude Corrosion Allowance)

      • Groove Repair - This method usually used for cracks and pinhole leakages. The section where leakage is present is grind down to a U or V groove. Weld metal is then deposited to restore the surface.
  • Additional Considerations
    • Materials 
      • SS Cladding/Plate lining to P3, P4, P5 materials tends to crack when excessive heats are applied during welding. Check for delayed cracking with UT 24h after job completion.
      • Hydrogen service vessels shall be outgassed and checked for its hardness after welding
    • Post Weld Heat Treatment
      • Check whether if vessel to be repaired require PWHT during fabrication. If yes, PWHT shall also be applied during repair in compliance to latest edition of ASME VIII Div 1 requirements (or refer to MDR). PWHT by oven is unlikely for in-service vessels however the following are usually used
      • Local banding PWHT
      • Preheat in place of PWHT
      • Controlled Deposition Welding in place of PWHT

Check API 510 Section 8 for the full requirements of PWHT by alternative methods, as there are certain material tests which needs to be performed, certain requirements to welding procedures on top of ASME IX WPS/PQR requirements, certain requirements for temperature, certain requirements for welding electrode type and not forgetting material considerations.

For additional repair procedures and guidelines on top of API 510, refer to ASME PCC-2.

Thursday, February 19, 2015

5.1 Plant Maintenance: Static Equipment and typical maintenance jobs

What are Static Equipment?
Basically these are the equipment that do not have a prime mover driven rotating component will be considered a static equipment, and here's some example with what sort of Offline/On-line preventive maintenance which are usually carried out on the static equipment. Corrective maintenance will be discussed at the end of this post, as it is what we wish to avoid.

Piping & Typical PM jobs: 
- Thickness monitoring(5y or less, depending on code used API570:Piping or API580:RBI)
- Visual Inspection (1y or less)
- Insulation reconditioning (When necessary)
- Painting (1y or more, depending on visual inspection)
- Pressure testing (Usually 10y or less, if critical or national code requires)
Source: Wikipedia


Pressure Vessel & Typical PM jobs: 
- Thickness monitoring(10y or less depending on code used API510:PV or API580:RBI)
- External Visual Inspection (1y or less)
- Internal Visual Inspection (half est. remaining life of the vessel, if remaining life is less than 4y internal inspection shall be every 2y)
- Insulation reconditioning (When necessary)
- Painting (1y or more, depending on visual inspection)
- Pressure testing (Usually 10y or less, if critical or national code requires)
- Types of inspection may vary if the vessel operates in potentially damaging susceptible services
Source: Wikipedia


Above ground tanks & Typical PM jobs: 
- Thickness monitoring(10y or less depending on code used API653:AGT or API580:RBI)
- External Visual Inspection (1y or less)
- Internal Visual Inspection (12y or less, unless with internal lining or leak detection installed)
- Insulation reconditioning (When necessary)
- Painting (1y or more, depending on visual inspection)
- Types of inspection may vary if the vessel operates in potentially damaging susceptible services
Source: Wikipedia


Heat exchangers & Typical PM jobs: 
- Thickness monitoring(10y or less depending on code used API510:PV or API580:RBI)
- External Visual Inspection (1y or less)
- Internal Visual Inspection (half est. remaining life of the vessel, if remaining life is less than 4y internal inspection shall be every 2y)
- NDT Inspection, WFMPI, eddy current, ultrasonic leak test (when leaks are suspected, or when service is critical, in corrosive media)
- Insulation reconditioning (When necessary)
- Painting (1y or more, depending on visual inspection)
- Pressure testing (Usually 10y or less, if critical or national code requires)
- Types of inspection may vary if the vessel operates in potentially damaging susceptible services
Source: Wikipedia


Distillation/Absorption columns & Typical PM Jobs
- Thickness monitoring(10y or less depending on code used API510:PV or API580:RBI)
- External Visual Inspection (1y or less)
- Internal Visual Inspection (half est. remaining life of the vessel, if remaining life is less than 4y internal inspection shall be every 2y)
- Insulation reconditioning (When necessary)
- Painting (1y or more, depending on visual inspection)
- Pressure testing (Usually 10y or less, if critical or national code requires)
- Tray/Packing replacement (Usually 2y or more, depending on manufacturer design or efficiency)
- Types of inspection may vary if the vessel operates in potentially damaging susceptible services
Source: Wikipedia


Reactors & Typical PM Jobs
- Thickness monitoring(10y or less depending on code used API510:PV or API580:RBI)
- External Visual Inspection (1y or less)
- Internal Visual Inspection (half est. remaining life of the vessel, if remaining life is less than 4y internal inspection shall be every 2y)
- Insulation reconditioning (When necessary)
- Painting (1y or more, depending on visual inspection)
- Pressure testing (Usually 10y or less, if critical or national code requires)
- Catalyst replacement (Usually 2y or more, depending on manufacturer design or efficiency)
- Types of inspection may vary if the vessel operates in potentially damaging susceptible services
Source: Wikipedia

Separators vessels & Typical PM Jobs
- See Pressure vessel above.
Source: Wikipedia


Steam traps & Typical PM Jobs
- Downstream steam check (1y or less, Live steam (faulty), lazy steam(working))
- Ultrasonic testing (1y or less, functionality check)

Source: Spirax Sarco

Manual Valves/Pressure relief valves & Typical PM Jobs
- These are usually done offline during shutdowns, unless the valves can be positively isolated for removal.
- Refacing of valve seat/trim
- Repacking of seal
- Replacement of corroded/ parts
- Overhaul of soft kit/spring/actuator/etc
- Overpressure test (MV), Set pressure test (PRV)
 

Source: Wikipedia

Note: About positive isolation - Positive isolation is done for safety reasons, usually either by closing two valves both up/downstream OR closing one valve with a blind installed both up/downsteam, to prevent any passing process media from escaping when maintenance works are carried out.

Valves are usually neglected by operators, they operate these valves using pipe wrench of various sizes. The huge torque applied with this leverage tool usually will speed up damage of the seats and as a result we experience passing of process media. Therefore, positive isolation is good practice to protect maintenance workers.


Filters/Strainers
- Differential pressure monitoring (Frequently)
- Backflushing or cartridge replacement(See manufacturer's recommended interval and action)
Source: Spirax Sarco


What sort of Plant maintenance should be carried out?
Preventive Maintenance
These type of maintenance are pre-scheduled on the plant's CMMS (Computerized Maintenance Management Systems).  The benefits of having a preventive maintenance program is that, there will always be some work for the contractors to carry out (be it to clock time sheet or earn earn extra cash??) Okay, the real benefit is that the manufacturer/code/national recommended maintenance intervals can be practised and followed up, so as to prolong the equipment life.

Types of preventive maintenance for Static equipment
- As discussed above at the top of this post.
- This type of maintenance are carried out offline or on-line, depending on the type of plant operations adopted or code requirements which may or may not permit carrying it out on-line.



Corrective Maintenance
These type of maintenance are usually carried out because preventive maintenance is not well practised, due to natural causes, design flaws, operating not according to manufacturer's prescribed conditions and many more reasons.

Types of corrective maintenance for Static equipment
- Box-in/Leak-sealing of pinhole leakage on pipe/vessel/weldments
- Pipe Spool replacement of piping due to the above
- Vessel/tank repair by cladding, shell course replacement, lap patch, plate lining due to thinning
- Steam trap replacement due to malfunction
- Heat exchange tube plugging due to tube leakage
- Unplugging of catalyst/packing/trays/filters by manual intervention


*Source: All images are from Wikipedia.org, except steam traps from Spirax Sarco. All photos are taken from open sources educational sites which allows for their material to be shared. Credits are given to the rightful image owner in this statement. Please drop me a comment should you be the rightful owner of the image and would like to request compliance for credit to be given to you directly.