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Storage Tank Failure: Examples, Causes, and Prevention

The storage tank is a very important static equipment for the oil and gas industry to store fluids. Even though various codes and standards stipulate its design to avoid failure of storage tanks, still there are many incidents of storage tank failures. So, storage tank failure is not at all a new phenomenon. In this article, we will explore the causes of such tank failures and steps for prevention.

Types of Storage Tanks (API 650)

Storage Tanks can be classified on many bases based on service, based on construction, based on Pressure & Temp & based on the roof (Atmospheric Pressure). Here, We will list the storage tank types based on the roof construction.

  • Double-Deck Floating Roof Tanks (DDFR): Double-deck floating roof Tank has two layers of the deck that floats over the product inside the Tank. This type of Tank construction consumes too much material as the deck is double. But it is used only for highly volatile products.
  • Single Deck Floating Roof (SDFR): Single deck floating roof Tanks are similar to DDFR; the only difference is the deck that floats is single. It uses bouncy for this type of Tank to maintain floatation.
  • Cone Roof (CR): Cone roof Tanks have a Cone roof. The roof slope is subject to the designer but 1:100 is common practice.
  • Internal Floating Roof (IFR): Internal floating roof Tanks are basically a collaboration of deck and roof. So, these types of tanks will have a Deck as well as a roof. The type of deck can be any type it may be single deck or Double deck Pan type.
  • Dome Roof (DR):– Dome roof Tanks are almost the same as the Cone roof; the only difference is they would not carry any deck and the shape of the roof will be Dome type.
  • Click here to know more about various types of atmospheric storage tanks

Detailed indication and nomenclature of roof-type storage tanks could be seen in Fig 1. Normally storage tanks fail in any one of the locations mentioned in Fig. 1.

nomenclature of roof type storage tanks
Fig. 1: nomenclature of roof-type storage tanks

Common Causes of Storage Tank Failures

Various studies conclude that majority of the storage tank failures are due to any one or combination of the following causes:

  • Corrosion: Most Common cause of storage tank failures
  • Improper Construction
  • Poor Maintenance
  • Incompatibility of fluid with the tank wall
  • Dispensing problems
  • Lack of Physical Safety i.e, Internal/External forces or events (Flood, fire, impact, etc.)
  • Excessive Pressure due to overfilling of Storage Tanks
  • Age/UV-related issues with non-metallic tanks
  • Failure of Pressure Vacuum Relief Valve (PVRV)
  • Seismic design failure
  • Scada failure
  • overturning because of Wind girder
  • Sabotage
  • Operational Errors on human interference
  • Violent weather changes

Types of Storage Tank failures

Storage tank failure modes can again be divided into various types such as

  • failures based on Pumping,
  • based on Material,
  • based on service,
  • Mechanical, civil, or electric failure, etc.

You will get many references for storage tank failures over the net caused by corrosion, improper construction, poor maintenance, etc. We will explain a few storage tank failure examples based on Mechanical Failure.

Storage Tank failure due to Overfilling

In the Guru Gobind Singh Refinery, India (2012), the refinery was handed over for commissioning after the completion of all necessary details. Because of the inadequate time frames and some construction requirements, water was filled into a big tank so that water could be used for hydro testing of other Tanks.  It was evening time and the operational people had to go for a shift change. But without informing the other relevant people on the next shift, the responsible person took the bus. So naturally, the valve is not closed. The Tank is filled totally and started overflowing but the overflow rate was not able to control the Pump flow rate. Within a short time span the tank failed, the rafter damaged the roof, the Deck stuck on the top & Weld of the plates of the lower thickness of the upper side gets sheared.

Tank failure example
Fig. 2: Tank failure example

Storage Tank Failure due to failure of the PVRV breaker

In the Sulfur Recovery Unit of the same refinery, one tankage failure incident occurred during commissioning. This failure occurred because of PVRV failure. The operator opens the valve to pump out but because of the PVRV failure, the Tank gets collapsed. Within seconds the tank explodes like a bomb. The products were water and so spreading around didn’t affect them much.

Root cause analysis shows that the PVRV installation had not been cross-checked. Because as per API 650, it’s not necessary to install a pressurized part during Hydro Testing because it’s just like the Water fill test in ATM pressure Tanks.

The following Fig. 3 explains the stage-wise incident of the storage tank failure.

Stage wise explanation of storage tank failure due to PVRV failure
Fig. 3: Stage-wise explanation of storage tank failure due to PVRV failure

Reason for Failures-

The most common reason for storage tank failure is the lack of knowledge, training, and inspection. In both of the above-mentioned failures, it was found that in both cases operator was not well-trained. The first failure is solely the mistake of the operator. In the second one, it was a PVRV failure but if we check the PVRV before every operation it can save the equipment and human lives. The second failure was in small diameter tanks (9 m diameter) as we can see in Fig 3. it was 9 m dia tanks. We could easily imagine the fatality if the tank diameter was larger.

The root cause analysis is performed to find out the root reason for what happened. After that, the finding is documented in the Lessons learned register for future reference to eliminate the reason for failure in future projects. In this article, we can understand the root was a lack of training & PVRV (supporting) equipment failure.

To make the lesson learned register, help from SME (subject matter expert) can be taken. They will guide and help to document the basic reasons for failure.

Prevention of Storage Tank failures

Failure of Storage Tank systems can be reduced by the following methods.

  • All necessary mounting shall be TPI (Third Party Inspection) inspected. Even after FAT (Factory acceptance test) they should be checked at the construction site by the Engineer in charge or in the presence of the Engineer in charge.
  • PVRV (Pressure vacuum relief valve) is something that is commonly used. It should be frequently checked during the operation.
  • All Tankages shall be protected by the emergency vent system.
  • All Tankages shall be inspected periodically.
  • The design of the Firewall and bund wall should be considered for contingency reserves.
  • External roof supports/self-supporting roofs
  • The design of tank thickness has to be proper
  • Proper Metallurgy of the used compatible material to reduce corrosion

Code and Standards for Tank inspection to reduce storage tank failures

The following codes and standards provide guidelines for inspection to reduce the failure probability

  • API 575 – Inspection of Atmospheric and Low-Pressure Tanks
  • API 653 – Tank inspection, repair, alterations, and reconstruction
  • API 570 – Piping Inspection Code
  • UL 142 – SteelAboveground Tanks for Flammable and Combustible Liquids
  • STI SP001 – Standard for Inspection of Above-ground Storage Tanks

Reference and Further Study:

Camouflaging of Oil Storage Tanks

The term Camouflage is widely used in the defense industry. Camouflage means using any combination of color, materials, or illumination for concealment. In recent times, the same painting technique is used by various countries to conceal the oil storage tank locations.

Camouflage for tanks is the painting technique or procedure that is used for confusing others to save the Oil Storage Tanks from air attacks during any war situation. The whole process is subjected to the art of color as well as the application of paint. Refer to Fig. 1 which shows an example of camouflaged oil storage tanks.

Camouflaged oil storage tanks
Fig. 1: Camouflaged oil storage tanks

Reason for Camouflaging

Tank Camouflaging is done to save Tanks from attacks. Environmental friendly color is added to tanks such that it matches with the nearby environment, thereby making them difficult to locate. Same as lizards changing their color to make us confused about their exact location. Army Tankers and their dresses are also camouflaged environmentally.

Camouflaging Colors

Normally used colors are terracotta, sea green, and yellowish color. There is no straight answer to this question it’s purely subject to client specification and the particular environment where Tanks are located on.

Codes and Standards for Camouflaging Tanks

The governing codes and standards used for tank camouflaging vary from country to country. A few of the codes and standards used are listed below for reference:

  • BS-4232
  • IS-5
  • IS-101
  • IS-161
  • IS-2074

Tank Camouflaging Methods

Camouflaging on tank surfaces can be done by following methods:

  • Manual Method using a brush
  • Using a roller or any traditional method
  • Air spray.

Disruptive painting for tank camouflaging shall be done in three colors in the ratio of 5:3:2 (all Matt finish)

  1. Dark green or sea green-5
  2. Light green -3
  3. Dark medium brown-2

Once the camouflaging is done, the tank is inspected and tested as per

  • Surface preparation test
  • DPT measurement
  • Crosscut test
  • Peel off test or
  • Holiday test

Cost Impact of Camouflaging

It increases your labor cost and decreases risk. As cost is directly proportional to risk obviously budget &  safety both shall be increased.

A few of the organizations that perform the tank camouflaging in India are:

  • Asian paints,
  • Burger paints,
  • Caroline,
  • Polucoates,
  • Bombay paints,
  • Nerolac paints,
  • Shalimar paints,
  • Sigma paints, etc

Click here To know more about tanks and related design details

Difference between API 650 and API 620 Tanks: API 650 vs API 620

What is API 650 Tank?

Tanks or Storage Tanks that are designed following the rules and guidelines of API 650 codes are API 650 Tanks. API 650 is the governing code for Welded tanks for Oil storage normally operating in the atmospheric pressure range. The code API 650 provides guidelines for the design, fabrication, material, erection, and inspection of welded vertical and cylindrical storage tanks. Such Tanks must be above ground with a closed or open top.

API 650 Tank
Fig. 1: API 650 Tank

What is API 620 Tank?

API 620 covers the design and construction of field-assembled large storage tanks operating in the low-pressure zone. Normally, API 620 tanks have more design pressure as compared to API 650 tanks.

Typical API 620 tank
Fig. 2: Typical API 620 Tank

In this article, we will study the major differences between these two types of tanks i.e. API 650 vs. API 620

Similarities between API 650 and API 620 Tanks

  • Both tanks are used for storage purposes.
  • Both API 620 & API 650 Tanks can be constructed from carbon steel, austenitic stainless steel, and nickel alloys (low temperature only).
  • A Welding Certification is stipulated by the American Society of Mechanical Engineers (ASME), Section 10 for both tanks.
  • For both tanks, a Non-Destructive inspection is required but a third-party inspection is not required.

Differences between API 650 and API 620 Tanks: API 650 vs. API 620

The major differences between API 650 and API 620 tanks are produced below in a tabular format.

ParameterAPI 650 TanksAPI 620 Tanks
DescriptionAPI 650 provides guidelines for Welded Steel Tanks for Oil StorageAPI 620 provides guidelines Design and Construction of Large, Low-Pressure Storage Tanks
ConfigurationThe configuration of API 650 tanks is Ground-Supported Bottom, Open or Closed RoofAPI 620 tanks can be of any configuration that has a single centered, vertical axis of revolution
ConfigurationFor API 650 tanks, the entire tank bottom has to be uniformly supported.API 620 tanks must have a single vertical axis of revolution.
Shop/Field ErectedTanks designed by API 650 can be Shop Fabricated (Appendix J) or Field Erected.API 620 tanks are Field Erected
Tank SizesAnyTank size larger than 300 ft.
Temperature RangeThe usual temperature range for API-650 tanks is -40 Deg. F to 500 Deg. FThe usual temperature range for API 620 tanks is -325 Deg. F to 250 Deg. F
Maximum PressureThe maximum pressure for API 650 tanks is 2.5 psig (pounds per square inch gauge) or 17.2 KpaThe maximum pressure for API 620 tanks is 15 psig
MaterialsCommon materials for API 650 tanks are Carbon Steel, Austenitic Stainless Steel, Duplex Stainless Steel, AluminumAPI 620 tanks are usually made of Carbon Steel, Austenitic Stainless Steel, and Nickel Alloys (Low Temp only)
Uses/IndustriesAPI 650 tanks are used for Oil, Gas, Chemical, Water, and Biofuel storage. A maximum of the most common welded steel tanks used in industry are designed following API 650. Tanks are typically found in Refinery tank farms, Terminals, Pipelines, and other process facilities use these tanks.Tanks like LNG tanks or Cryogenic tanks which require high internal pressure are designed as per API 620.
Table: API 650 Tanks vs. API 620 Tanks

Few more related articles for you.

A Brief Presentation on Storage Tanks
Various Types of Atmospheric Storage Tanks
Tank Settlement for Piping Stress Analysis
Considerations for Storage Tanks Nozzles Orientation
Equipment and Piping Layout for Storage Tanks
Case Study of Tank Farm Design and Dike Wall Height Calculation

Design of Bolted Connections or Bolted Joints

Bolted joints are one of the most common elements in piping design. Whenever flanged joints are used, bolted connections play an important role in keeping flanges together and avoiding flange leakage problems. So Bolting is an important component of piping systems.

In general, Boltings seem petty things for a whole lot of piping system design. Therefore, they tend to be “forgotten” when it comes to detailing their features, especially the length.

It is true that with nowadays technology of 3D modeling, it will be automatically calculated. However, this is only applicable when it is a normal joint consisting of Flange-Gasket-Flange. In some other cases, Piping Engineers need to put more attention to details and define the length manually.

It would be one of the “failures” if these lengths cannot be rectified upfront and only discovered when installation comes in hand. Imagine if you are doing a big-scale project, it will definitely delay the progress. And unfortunately, just because of these “petty” things.

Let’s see what are the bolting design features that Piping Engineers required to define and check in order to have technically complied boltings.

Bolting Features to be Checked in Bolted Connection

While deciding on a bolted joint or bolted connection the following bolting design features must be thoroughly checked to ensure a leak-free long-lasting piping system.

  1. Service – Defining Bolts Material
  2. Size & Quantity
  3. Washer Requirement
  4. Inline Items
  5. Length
  6. Coating – Common practice

Fluid Service to Define Bolt Materials

Like any other piping items, the bolt material will be based on the service that they will be used for. This will be defined when Piping Engineers are preparing their Piping Material Specifications. No ratings are required for boltings as they are not pressure-containing parts.

Other than the OWNER’s specification and requirement, another reference that can be taken into account is API 6A. Below attached is an example and guideline on boltings material to be used based on its service;

Bolting Material guidance as per API 6A
Fig. 1: Bolting Material guidance as per API 6A

ASME B16.5 also showed materials for boltings as below;

ASME B 16.5 Bolting Material Guidance
Fig. 2: ASME B 16.5 Bolting Material Guidance

Size and Quantity of Bolts

The size of the boltings will relate to the size of the flange, and quantity will relate to the flange rating. Flange with sizes from 1/2″ up to 24″ will refer to ASME B16.5 and ASME B16.47 for larger sizes. From the table, the size, quantity, and standard length (normal joint of Flange-Gasket-Flange) will be provided.

The length would largely depend on the Flange class rating as the thickness of the flange differs when the rating increase. Examples of Class 150 and Class 300 are shown in Fig. 3 and Fig. 4 below;

Bolt Lengths for ASME Class 150 flanges
Fig. 3: Bolt Lengths for ASME Class 150 flanges
Bolt Lengths for ASME Class 300 flanges
Fig. 4: Bolt Lengths for ASME Class 300 flanges

This length has been calculated with all considerations as in Nonmandatory Appendix C. We will cover this calculation again.

Washer Requirement for Bolted Connections

A common practice the boltings do not require a washer. Thus, when will washers be required? Washers in bolted joints are used:

  • When used with an insulation gasket kit. This is to provide an engagement grip to the non-metal washers.
  • When the non-metal flange is used to avoid flange damage due to the force exerted.
  • Special case if the bolt holes are bigger and may cause loose boltings.

Type of Washers

ASME B18.21.1 provides the following types of washers:

  • Plain (Flat) Washers
  • Helical Spring Washers
  • Tooth Lock (Internal, External) Washers
Washer types per ASME B18.21.1
Fig. 5: Washer types per ASME B18.21.1

Bolting considerations for Inline Items

Normal flange joints will consist of Flange-Gasket-Flange, and usually by 3D modeling setup; this has been auto-calculated to define the length of the bolt. However, whenever inline items involved Vendor data incorporation, it is wise to check manually and implement it inside the 3D setup. Actual thickness to be incorporated to avoid the insufficient length of the bolt.

Examples of inline items that require Final Vendor Data to be incorporated;

  1. Valves (manual & control valves) – sometimes its end-to-end dimension as per Manufacturer’s Standard.
  2. Gaskets – especially insulation gaskets, the thickness may exceed the standard 3 mm that the usual 3D system would assign for spiral wound gasket (after compressed). Extra care for a joint that consists of multiple gaskets joint.
  3. Spade, Spacer, Spectacle Blind
  4. Instrument Items – other than Control Valves, all instrument items that are connected to piping shall be checked. Sometimes it came with non-standard flange thickness or upper-Class rating that requires an extra length of bolts.

Bolt Length Calculation and Considerations

Appendix C of ASME B16.5 provides an example of how the bolt length has to be calculated and what considerations need to be taken;

Bolt Length Calculation for Bolted Joints
Fig. 6: Bolt Length Calculation for Bolted Joints

For the size of bolts more than 1″, the bolt tensioning requirements shall also be considered. For this, add another 1D or 1 thickness of nut for the total length.

The following Bolt tensioning video tutorial explains clearly the requirement of the above-mentioned 1D or 1 thickness of the nut.

Video Tutorial: Bolt Tensioning Requirements

Bolt Coatings on Bolted Connections

Coatings on bolts can be said quite common nowadays. Even some OWNER would specify ALL bolts shall be coated. As stated before, even though bolts are seemed petty, non-pressure-containing parts; bolts will be sitting in the weather dry and wet maintaining the force of tightening for the pressure-containing parts. To ensure the strength are efficient, corrosion is one of the major things to be avoided.

The most popular coating that is used is Fluorocarbon Coating (Xylan, PTFE, Teflon).

But, there were other types of coatings such as;

  • Galvanized (Hot Dip, Mechanical)
  • Electroplating (Cadmium, Zinc)

It is important to ensure the requirement of the project on the bolt coating. Some projects may be delayed just because this one little thing (but important) has been missed out of consideration.

Few more related articles for your consideration.

Guide for Coating Selection for External Bolting to Reduce Corrosion
How to Select a Bolt: A definite Guide
Difference between ASME B 16.47 Series A and Series B Flanges
Collar Bolts To Maintain Removable Bundles in Heat Exchangers
Methods for Checking Flange Leakage

What is a Pipe Expansion Joint and Why do I need one?

Piping Expansion Joints or Expansion Bellows are highly engineered mechanical devices containing one or more metal/rubber bellows. Expansion Joints are used to absorb dimensional changes caused by thermal expansion or contraction of a pipeline, duct, or vessel while containing the system pressure. The flexible element of the expansion joint that expands or contracts to absorb thermal movement is called Bellows. It consists of one or more convolutions. Expansion joints are successfully used in Refineries, Chemical and Petrochemical Plants, Cryogenic plants, Nuclear power plants, Automotive, Aerospace, and heating & cooling systems.

Piping Expansion Joints
Fig. 0: Piping Expansion Joints

Why Install Piping Expansion Joints?

Piping Expansion Joints serve various purposes when installed in a piping system. Those are:

  • To absorb movement (Thermal expansion as well as compression)
  • To relieve system stress and strain.
  • To reduce mechanical noise and vibration.
  • To have a compact design (space constraint)
  • To compensate for misalignment.
  • To eliminate electrolysis between dissimilar metals.
  • To reduce piping loads on equipment nozzles.

Components of an Expansion Joint

The main components which constitute an expansion joint are as follows:

  • Bellow
  • Tie Rods
  • Flanges
  • Shipping Bar
  • Protective Covers and Internal Liners
  • Special Attachments like Pantographic linkages, etc

Refer to Fig. 1 which shows the main elements of a piping expansion joint.

Components of an Expansion Joint
Fig. 1: Components of an Expansion Joint

Bellows:

Bellows are the most important element of a piping expansion joint. This is the basic unit of every expansion joint. They are of two types:

  • Formed Bellows
    •  Formed from a thin-walled tube
    •  Contains only longitudinal welds
    •  Single & Multiply
  • Fabricated Bellows
    •  Series of thin gauge discs welded together
    •  Uses heavier gauge materials than those formed bellows

Regardless of the manufacturing method used, all bellows consist of the same basic components as shown in Fig. 2. Bellows can be single-ply or multi-ply designed.

Basic Components of Bellow
Fig. 2: Basic Components of Bellow

Additional components are added to bellow to create expansion joints of increasing complexity and capability which are suitable for a wide range of applications.

Tie Rod of Expansion Joint:

As the name indicates, Tie rods are basically bars or rods, attached to the expansion joint assembly. Tie rods are designed to absorb pressure loads and other extraneous forces like dead weight. Sometimes, Tie rods (Fig. 3) are used as Limit rods to protect the bellows from movements in excess of design that occasionally occur due to plant malfunction or the failure of an anchor.

Tie rod and Limit rod of a piping expansion joint
Fig. 3: Tie rod and Limit rod of a piping expansion joint

Expansion Joint End Connections:

Three types of end connections (Fig. 4) are available in a piping expansion joint to attach it to a piping system. They are

  • Flanged End including Special flanges, slip-on, or angle flanges.
  • Vanstone Ends are a type of modified flanged ends that adds flexibility and resolves bolt-hole misalignment.
  • Welded ends: Any pipe or duct can be directly welded to such bellows.
Expansion Joint End Connections
Fig. 4: Expansion Joint End Connections

Protective Covers and Liners for an Expansion Joint:

The expansion joint components are put inside a metallic cover to protect them from external sources as shown in Fig. 1.

A liner is provided to minimize the effect of flowing media on the bellow inner surface. Refer to Fig. 5.

Protective Cover and Liner
Fig. 5: Protective Cover and Liner

Purge connections are provided along with internal liners to reduce the bellow’s skin temperature while using in high-temperature applications such as catalytic cracker bellows. Normal air or steam can be used as a purge medium. Purging helps in flushing out the particulate matter between the bellows and the liner. Harmful solids built up in the convolutions can also be stopped by purging.

Pantographic Linkages:

Pantographic Linkage is a scissors-like device that is a special form of control rod attached to the expansion joint assembly. They are used to positively distribute the thermal movement equally between two bellows of the universal joint throughout its full range of movement. However, note that they are not designed to restrain pressure thrust.

Pantographic Linkages
Fig. 6: Pantographic Linkages

Types of Expansion Joints

Broadly Piping Expansion Joints can be grouped into two categories:

  • Unrestrained Expansion Joint and
  • Restrained Expansion Joints

Unrestrained Type Expansion Bellows:

Unrestrained Expansion joints are assemblies not capable of restraining the pressure thrust of the system.  So, The pressure thrust must be contained using main anchors or equipment. They are of the following types:

1. Single Expansion Joint Assemblies are the simplest type of expansion joint consisting of a single bellows element welded to end fittings, either flange or pipe ends. 

2. Universal Expansion Joint Assemblies consist of two bellows connected by a center spool piece with flange or pipe ends. The main advantage of a universal expansion joint over a single expansion joint is that the universal arrangement provides greater absorption of axial, lateral, and angular movements than a Single Expansion Bellows Assembly.

3. Externally Pressurized Pressure Balanced Assemblies are used when a large amount of axial movement is required to absorb and pressure thrust must be absorbed by the expansion joint. The opposing force balancing theory is quite similar to the In-Line Pressure Balanced Expansion joint Assembly. However, in the current case, the opposing forces are generated from pressure acting on the outside of the bellows.

Unrestrained type expansion joint
Fig. 7: Unrestrained type expansion joint

Restrained Type Piping Expansion Joints:

In Restrained type piping expansion joints, the expansion joint hardware is capable of restraining the pressure thrust of the system by their design.  Intermediate anchors are installed to withstand the spring force generated due to the deflection of the expansion joint.  The main anchors are not required. They are again of various types as mentioned below:

1. Tied Single Expansion Bellows Assemblies add tied rods to a Single Bellows Assembly to increase design flexibility in a piping system.  The tie rods are attached to the pipe or flange with lugs. These tie rods carry the pressure thrust generated in the system, eliminating the need for main anchors.

Externally Pressurized and Tied Bellows
Fig. 8: Externally Pressurized and Tied Bellows

2. Tied Universal Expansion joint Assemblies are mostly similar in construction to a Universal Assembly. The only difference is that tie rods absorb pressure thrust and limit movements to lateral offset and angulation only.

3. Hinged Expansion Bellows Assemblies limit movement to angulation in one plane. Hinged Assemblies (Fig. 9) are normally used in sets of two or three to absorb large amounts of expansion in high-pressure piping systems.

4. Gimbal Expansion Bellows Assemblies are designed to absorb system pressure thrust while allowing angulation in any plane. Gimbal Assemblies (Fig. 9), when used in pairs or with a Single Hinged unit, have the advantage of absorbing movements in multi-planer piping systems.

Hinged and Gimbal expansion joints
Fig. 9: Hinged and Gimbal expansion joints

5. Pressure Balanced Elbow Assemblies are used in applications where space limitations are a concern. A system of tie rods or linkages is used in such a fashion that the pressure thrust acting on the line bellows is equalized by the balancing bellows. The only forces transmitted to equipment are low spring forces created by the axial, lateral, or angular movements.  An elbow must be present in the piping network to install this style of expansion joint.

Pressure Balanced Elbow Assembly
Fig. 10: Pressure Balanced Elbow Assembly

6. In-Line Pressure Balanced Bellows Assemblies are used if a piping elbow is not present in a piping network to use the pressure-balanced elbow assemblies and pressure thrust has to be absorbed by the expansion joint. The inline bellows are tied in the expansion joint through a series of tie rods which equalizes the pressure thrust force. The opposing pressure forces cancel each other leaving only the low spring forces generated from the bellows deflection.

Inline Pressure Balanced Expansion Joint
Fig. 11: Inline Pressure Balanced Expansion Joint

Expansion Joint Materials

The selection of bellows material is another important factor to be considered in the design of a piping expansion joint. Some of the factors which influence the proper expansion bellow the material selection process are:

  • Corrosion Properties: Process media, surrounding environment, and internal cleaning agents.
  • Mechanical Properties: High-temperature service, cryogenic service, and operating stresses.
  • Manufacturing Properties: Forming and cold working capabilities and cost & material availability.

Expansion Joints are available in metallic and non-metallic materials. The most common expansion joint materials, widely used in the piping industry are:

Expansion Joint Design Codes and Standards

Expansion Joints used in industry are designed, manufactured, and tested in accordance with the following Codes and Standards

  • EJMA, Expansion Joint Manufacturer Association, Inc.
  • ASME B31.3 Appendix X, Metallic Bellows Expansion Joints
  • ASME Sec. Ⅷ Div.1, App.26.
  • EN 14917 Metal Bellows Expansion Joints for Pressure Applications

Expansion Joint or Bellow Manufacturers

There are many organizations that produce piping expansion joints. few of the most reputed expansion joint industry leaders are:

  • U. S. Bellows
  • Piping Technology and Products
  • Garlock
  • SFZ
  • Senior Flexonics
  • Hyspan
  • United Flexible
  • Mega-Flexon
  • Triad Bellows
  • Metraflex, etc.

Click here to know more about the conditions when an expansion joint in piping systems is required and the design considerations for piping expansion joints.

Steam Trap Installation Best Practices

Steam traps are very essential in power piping as these devices remove unnecessary condensate from the steam lines. A steam trap serves two basic purposes:

  1. Separate the condensate from the steam as quickly as it is generated and
  2. Stop the stream discharge.

Every steam systems normally employ many steam traps at strategic locations to avoid the condensate to mix with the steam and create a two-phase flow. The steam condensate two-phase flow can damage the piping, supports, or even the connected equipment if not removed. Thus steam traps play a major role in plant safety.

In this article, we will discuss the best practices for steam trap installation.

Steam trap Installation Best Practices

Studies have shown that incorrect steam trap installation creates a high percentage of steam trap failures. Certain faulty installation negatively impacts the steam trap performance. As per process heat transfer considerations, A properly installed steam trap needs

  • a 24-in. minimum from the steam supply line to the steam-trap inlet and
  • an 18-in. maximum from the vertical leg to the steam trap as shown in Fig. 1 below.
Minimum distances of steam trap assembly
Fig. 1: Minimum distances of steam trap assembly

Experiences showed that a properly installed steam trap should efficiently work for six years without any maintenance.

A few of the Steam trap installation best practices are outlined below:

Ensure Gravity Flow:

The most important rule to remember for steam-trap installation is one of Mother Nature’s Laws — Gravity (Fig. 1). Installation should ensure the condensate flow from the process to the steam trap by the gravity forces. Pressure and velocity can not be relied on to remove the condensate from the process.

Ensure Steam Leakage Rate of Steam Traps:

For the Steam Traps that are being purchased, determine the steam leak rate following the leak rate standards mentioned below:

  • a. PTC-39
  • b. ISO 7841

A quantifiable amount of steam always leaks through the steam traps. Hence, The selected steam traps must ensure that steam traps with the least amount of steam loss are specified. Such Steam Traps will prevent unnecessary energy loss.

Threaded Connections:

Steam traps with 1 in. or smaller connections should use tubing with tube connectors. Such an arrangement will avoid leak points (for example, threaded connections). Traditionally, threaded connections are obvious sources of leaks in the system due to expansion, contraction, and corrosion that occurs in a steam system. Refer to Fig. 2.

 Steam-line drip-leg steam-trap installation using tubing and tubing connectors
Fig. 2: Installation of Steam-trap using tubing and tubing connectors

Material Pressure rating:

Tube connections for steam trap installations are available from numerous steam-component manufacturers. Before placing an order ensure that the pressure ratings of the component material are acceptable.

The piping connection from Process to Steam Trap:

The Piping from the steam trap to the process connection shall be equal to or larger than the process outlet connection. Hence, it is suggested not to reduce the piping/tubing diameter before the steam trap or reduce the connection size of the steam trap. For example, a steam unit heater with a 1-in. condensate outlet would require 1-in. or larger piping/tubing from the unit heater to the same connection size on the steam trap.

Piping Connection Downstream of Steam Trap:

The pipe/tube diameter downstream of the discharge connection of the steam trap should be expanded. For example, 1-in. (connection) steam-trap discharge tubing/piping should be increased to 1.25 in. or 1.5 in.

Universal Mounts:

Universal mounts shall be used for connecting the steam trap devices with a connection size of 1 in. or smaller to the tubing or piping. With the universal mount, the steam trap is connected to the application with two bolts. This reduces the time required for the installation of the steam trap.

Use of Strainer:

Including a strainer as part of the steam trap installation is always suggested. The strainer can be accomplished by the following:

  • a. External strainer ahead of the steam trap
  • b. Steam trap with integral strainer
  • c. Universal mount with an integral strainer

Premature Steam trap failures due to corrosion will be eliminated by the strainer.

When installing an external or internal strainer, always install a blow-off valve on the strainer. This allows the strainer to be blown down during operation and, more importantly, permits the steam trap cavity to be safely depressurized during service.

Some other important Steam trap Installation Best Practices are:

  • The steam trap should be installed in an accessible location.
  • A visual indication (can be a sight glass or test valve) of the steam trap performance shall be installed on all process applications.
  • Always locate the steam trap below the lowest condensate discharge point of the equipment.
  • Ahead of the steam trap, A rise in pipe elevation is not at all desirable.
  • In most applications, check valves are installed after the steam traps.
  • Installation standards for all applications shall be maintained for future reference.
  • ASME B31.1 code is normally followed.

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