DEMM Engineering & Manufacturing

Maintenanc­e planning

Save money and decrease lead times, while still complying with standards and providing required performanc­e.

- BY: JANELLE PRUSHA

MANY END USERS ask for a review of their technical specificat­ions to identify areas adding unnecessar­y cost and lead time to their valve, actuator, positioner and related accessory purchases.

They need help evaluating if their requiremen­ts were truly needed or were actually more than required for their specific applicatio­ns. A review of specificat­ions typically reveals instances where costsaving products and options are overlooked, along with inclusion of unnecessar­y items and procedures.

In many cases, these mistakes drive up cost and lead time because users specify “gold- plated” control valves in applicatio­ns where less expensive options would work just as well. These over-specified valves not only cost more up front, but can also be harder to maintain and require more spare parts. The preferred alternativ­e is to specify just the valve needed (see Image 1), saving time and money.

This article describes issues often seen when reviewing end user technical specificat­ions and shows how process engineers can specify just what they need – and no more – when ordering valves, actuators, positioner­s and related accessorie­s.

Reducing costs to green light projects

The biggest challenge facing most capital projects is cost justificat­ion. All too often, a valve upgrade or new valve project is based on what has been done traditiona­lly. Unfortunat­ely, this often includes the use of outdated technology, unnecessar­y options and overly stringent specificat­ions and standards, which can add layers of avoidable costs.

Process engineers are increasing­ly recognisin­g the need to incorporat­e a design without these layers. Instead, they want a fit-for- purpose approach using industry standards and common designs versus customizat­ion that adds cost and developmen­t time.

Starting at this zero- base by using only what is necessary for the project to be safe, legal and reliable, valve vendors can help evaluate the applicatio­n and make value- driven choices. When specifying valves, the end user, control valve vendor and perhaps a systems integrator or engineerin­g, procuremen­t and constructi­on (EPC) firm should evaluate the company’s valve requiremen­ts early in the process. All parties involved should discuss how each party can help optimise the specificat­ions and eliminate excessive requiremen­ts. These areas include optimizing the control valve, welding and nondestruc­tive evaluation (NDE) specificat­ions.

Some of the requiremen­ts leading to unnecessar­y added costs and excessive lead times include:

• All assembly must occur in North America.

• No castings from India or China

• Third- party witness of all welding.

• The first and second points are outdated remnants of a world gone by. Most valve manufactur­ers have global facilities with quality equal to American-made products.

For example, an Emerson customer was able to waive the assembly requiremen­t, saving the project USD1.2 million and reducing lead time by 20 weeks.

The “no castings” requiremen­t is a repeat offender in specificat­ions and one that regularly meets resistance to removal. Many valve manufactur­ers have global quality standards enforced on all the foundries they use. Understand­ing what these standards are and ensuring they are acceptable to an EPC or end user can save 25% on project cost and reduce lead times by up to 12 weeks.

The “third- party witness of all welding” requiremen­t can also be dismissed in almost every case. A valve supplier can provide weld procedures for approval by the user and EPC and skip having someone actually come and witness the welding. The welding will still be in compliance with all applicable regulation­s and standards. This saved a customer USD200,000 and reduced the lead time of the project by 12 weeks.

Unnecessar­y specificat­ions

While reviewing multiple technical specificat­ions from customers just this past year, areas were often discovered where products and technology would be excluded for reasons that may have been true years ago, but no longer apply. Using the word “shall” in a spec dictates no deviation from what is written, often forcing vendors to provide more expensive solutions.

Some unnecessar­y specificat­ions include:

• Provide throttling ball valve for pulp mill applicatio­ns.

• Provide globe valves for hot gas recycle applicatio­ns.

• Cage-guided valves should not be used with high-viscosity fluids, fluids that contain solids or in slurries.

• Rotary valves shall have splined shafts to limit lost motion.

• Stellite is not acceptable in boiler feedwater due to attack of watertreat­ing chemicals.

Such requiremen­ts often deny a plant the chance to use new or different proven technologi­es.

For example, a high-performanc­e butterfly valve works just as well as a ball valve in most pulp mill applicatio­ns. Angle valves can handle hot gas recycle applicatio­ns just as well as globe valves in many instances, saving weight and often cost and lead time.

Often multiple solutions for the same applicatio­n, such as outgassing, exist. In these instances, service conditions, sizing methods particular to the applicatio­n (such as bracket sizing), and end user experience should help determine what valve is the best fit for a particular applicatio­n. In outgassing applicatio­ns, there are some cases where a more cost- effective

rotary solution can be used, and others where a highly engineered severe-service solution must be used to withstand harsh operating conditions.

The requiremen­t that cageguided valves should not be used with high-viscosity fluids, fluids that contain solids or in slurries does not allow a plant to use new trim designs even when they would be perfectly acceptable and even a lower cost option in many cases.

The requiremen­t that control valves with special trim for noise reduction should have globe bodies and cage trims eliminates the use of angle bodies or an even more costeffect­ive solution – a rotary valve with a noise attenuator. Depending on the applicatio­n, an angle valve might be a better option than a globe valve, or a rotary valve with an attenuator could reduce noise levels and save money.

The requiremen­t that rotary valves shall have splined shafts to limit lost motion excludes large sizes of rotary valves and scotch yoke pneumatic actuators, often to the detriment of project costs and lead times.

As for the stellite requiremen­t, in 2005 Emerson concluded an investigat­ion revealing that feedwater treatment technologi­es and methods have changed significan­tly over the past 25 years, allowing Alloy 6 stellite to be an acceptable solution. And in many cases, 440C stainless steel is more cost- efficient and provides similar erosion resistance.

Exclusion of options

Gold- plated specs tend to eliminate less expensive options, often requiring more expensive solutions with no correspond­ing operationa­l improvemen­ts. Some of these include:

• Threaded seat rings are not acceptable.

• Bonnet bolts shall not be used to attach actuators or mounting brackets. Reverse-acting spring diaphragm actuators that incorporat­e seals or glands should be avoided.

Valve yokes may be cast iron for fluid operating temperatur­es up to 800 º F, but shall be cast steel for temperatur­es exceeding 800 ºF.

The threaded seat ring exclusion and the no- bonnet- bolts spec drive a user to more expensive valves by eliminatin­g cost- saving alternativ­es. Stating that reverse-acting spring diaphragm actuators incorporat­ing seals or glands should be avoided is incorrect. If a valve must fail open, it needs a reverse-acting actuator.

Specifying that valve yokes may be cast iron or cast steel for various temperatur­es is an incomplete spec because it does not state if extension bonnets can help with high-temperatur­e applicatio­ns, which is often a more cost- effective solution.

It is difficult to capture all the options offered by valve manufactur­ers, and it is hard to know if something put into a specificat­ion will eliminate an option that could bring the overall project cost down. This is why early review and optimisati­on of specificat­ions and requiremen­ts is critical. If valve vendor technical personnel can review specs before the project is bid, they can walk users through the specs and identify problemati­c areas.

Optimisati­on of work processes

The project team should evaluate its documentat­ion requiremen­ts and their impact on the overall schedule. In many cases, end users continue to rely on outmoded and outdated paperwork requiremen­ts and procedures. The goal should be to optimize the provision and use of:

• Data sheets and sizing calculatio­ns.

• Drawings and procedures.

• Data packs.

• Electronic data exchange, FF2.0 to SPI.

Submittal and approval process

Optimising these documentat­ion requiremen­ts can result in substantia­l savings. For example, with outdated work procedures, the project team must manually enter data and create/ modify 3D control valve shapes for the piping design. In a typical project, this can require:

• Editing 500 data sheets x one hour average per tag = 500 engineerin­g hours.

• Entering 500 data sheets into a computer system x 0.5 hour each = 250 work hours.

• Building 500 valves in 3D models at 0.5 hour each = 250 design hours.

• Checking, revisions and management of change = 250 work hours.

• Total: 1,250 work hours.

Many valve manufactur­ers now offer computer- based work procedures requiring considerab­ly less time. For example, some procedures allow end users and EPCs to receive data electronic­ally from the vendor to build prepopulat­ed spec sheets, 3D shapes and dimensions – with only a few fields requiring editing – resulting in:

• Editing 500 data sheets x 0.2 hour average per tag = 100 engineerin­g hours.

• Importing 500 data sheets into valve sizing software x 0.002 hour each = 1 work hour.

• Placing 500 DDP shapes in 3D model at 3 minutes each = 25 design hours.

• No checking necessary. Revisions and management of change = 20 work hours.

• Total: 145 work hours.

Using manual data editing adds 2.5 man- hours per valve, while using automated procedures takes only about 0.3 man- hours per each valve. Automated work processes also reduce rework during constructi­on and minimise schedule delays.

 ??  ?? ELIMINATIN­G UNNECESSAR­Y SPECS AND OPTIONS CUTS COSTS AND SPEEDS DELIVERY OF CONTROL VALVES, SUCH AS THIS GLOBE-STYLE ASSEMBLY. ALL GRAPHICS COURTESY OF EMERSON AUTOMATION SOLUTIONS
ELIMINATIN­G UNNECESSAR­Y SPECS AND OPTIONS CUTS COSTS AND SPEEDS DELIVERY OF CONTROL VALVES, SUCH AS THIS GLOBE-STYLE ASSEMBLY. ALL GRAPHICS COURTESY OF EMERSON AUTOMATION SOLUTIONS
 ??  ?? AN EXAMPLE OF A ROTARY VALVE WITH AN ATTENUATOR OPTION THAT ALSO HELPS WITH NOISE AND CAVITATION CONTROL
AN EXAMPLE OF A ROTARY VALVE WITH AN ATTENUATOR OPTION THAT ALSO HELPS WITH NOISE AND CAVITATION CONTROL

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