Tuesday, January 8, 2008

Why not bury flare pipe header ?


Flare and venting facilities is commonly provided in Oil and gas plant for proper disposal of hydrocarbon gas during plant black start-up, normal start up, operation, emergency relief and plant depressurization. A proper design would have elevated flare header sitting on pipe support and slopping down to flare / vent knock out drum (KOD). No low pocket is expected along the header.

There was a question raised.
Should a flare header buried in the soil ?

Advantages
The advantages of burying flare header are :
- Flare header is normally large in diameter and it needs a large and strengthened pipe support to elevate and maintain proper slopping of header to KOD. It is costly to provide a large support. Burying flare header would save cost on providing pipe support.
- Post hot gas relief to header follow by quick cooling by cold ambient would lead to shrinkage and potential air ingress into the flare header. By burying flare header, soil would act as an insulation layer to minimize heat lost and to minimize the potential of air ingress.

Problems
However, there are many problems associated with buried flare header. One of the problems is creation of low pocket between sources e.g. Pressure relief devices, Blowdown valves, etc and flare stack. Low pocket would promote liquid accumulation and it derives other problems with liquid accumulation.

Flame-Out & Gas Cloud
Whenever a large relief, high velocity vapor may push the liquid in the form of liquid slug towards flare tip. As flare tip is not designed to accommodate liquid slug, it potential put-off the flare and result flame-out condition. It may create gas cloud and potentially lead to severe explosion if it ignited.

“Fire Rain”
Flame-out is expected in the event large liquid slug passing flare tip. On the other hand, there is still possibility of ignition of liquid slug. Liquid on fire came out from flare tip would drop to flare stack support structure and lead to flare stack structure failure prematurely.

Surge and severe vibration
High velocity vapor from relief pushing accumulated liquid may cause severe slugging flow in the flare header. In addition, there is potential of generation of slug knocking at elbow and result severe surging to the flare header. Both will creates severe flare header vibration and potentially lead to header and support failure.

Internal corrosion
Accumulated liquid in flare header would promote internal corrosion and accelerate metal loss.

External corrosion
Normally a buried would be protected by corrosion protection layer. Damage of this protective layer is difficult or non-detectable and potential risk of external corrosion. Internal corrosion couple with external corrosion would even accelerate the corrosion and leak hole is easily formed. It will create hazard in the event gas leak during large relief.

HSE issue
Gas leak will result health, safety and environmental problem.

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Monday, January 7, 2008

Useful Documents Related to Pressure Relief Valve (PRV) - Part 3



This post is continue from previous posts :
a) Useful Documents Related to Pressure Relief Valve (PRV) - Part 1
b) Useful Documents Related to Pressure Relief Valve (PRV) - Part 2



Rigorously Size Relief Valves for Supercritical Fluid
by Ryan Ouderkirk
Previously published methods can be tricky to apply, and may lead to improperly sized valves. Here is a stepwise, detailed method that more-accurately determines the orifice area.

Select the best model for Two-Phase Relief Sizing
by Ron Darby and Paul R. Meiller
A variety of methods exist for sizing valves, but not all give the best predictions for certain conditions. This article discuss the available model and selection of them.

Sizing of Relief Valves for two phase flow in the Bayer Process
by Quoc-Khanh Tran and Melissa Reynolds
This paper is to review the methods currently used in engineering design calculations for predicting the relieving capacity of a safety relief valve under various entering flow conditions. The methods considered include the Recommended Practice (RP) 520 of the American Petroleum Institute (API), the Homogeneous Equilibrium Model (HEM) and various published empirical Slip Models

Transient Analyses In Relief Systems
by Dirk Deboer, Brady Haneman and Quoc-Khanh Tran
This paper will focus on the application of transient process analyses on the high pressure leach (or Digestion) area of alumina refineries. The impact of vessel blockages and plant power failures will be discussed with emphasis on analysis methodology for power failures.

Advantages and Limitations of Pressure Relief Valves Types
This article summarized Pressure Relief Valve (PRV) type advantages and limitations.

Practices for Pressure Relief Valve Discharge Piping
By Greg Uhrhan, P.E.
Many mechanical refrigeration systems containing large quantities of refrigerant possess pressure relief devices. Under certain conditions, these systems are piped to the outdoors to prevent the displacement of air inside a structure. This paper is intended to give a list of best practices for sizing the piping from the discharge of a pressure relief valve to the outside.

Why use a pilot valve ?
Austral Engineering
It is a common question asked amongst process engineers on why use a pilot valve for a particular application ? The following article I hope will answer this question and provide some insights into the different types of pilot valves available on the market today and their many features and benefits.

New Wireless Pressure Relief Valve Monitoring System Provides Significant Operational Benefits
Accutech
Pressure relief valves represent a significant threat to the goal of zero emissions. These devices relieve excess pressure in piping and vessels by venting process gas. The gas released normally is routed to the flare, to a recovery system or directly to the environment. All of these avenues are an environmental concern.

Wireless Instrumentation Determining Relief Valve Discharge
Accutech
Relief valves are designed to relieve pressure and provide safe operation. They typically function by opening at a given set pressure, venting, and then resealing when a safe pressure has been re-established. Very frequently, relief valves are installed in gas service and the gas is vented to the atmosphere or to a safety flare. These valves are frequently installed in remote locations where monitoring of the valves is difficult. The Accutech Wireless Acoustic Monitor simplifies the task of monitoring relief valves. The non-invasive installation of the Acoustic Monitor coupled with wireless transmission of data on the relief valve operation provides an easy and inexpensive monitoring solution.

Assessing Pressure Relief Needs
By Chip Eskridge, P.E.
Evaluating thermal expansion and overpressure protection.

Safety Relief Valves Replacement, Maintenance, Installation Recommendations
Henry Technologies
Safety relief valves are relatively maintenance free devices. Even so, we would recommend a periodic inspection of these devices every 6-12 months. A visual inspection should be made to verify the condition of the valves. While performing this inspection, some of the conditions to watch for are...

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Sunday, January 6, 2008

Useful Documents Related to Pressure Relief Valve (PRV) - Part 2


This is a continuous post from "Useful Documents Related to Pressure Relief Valve (PRV) - Part 1"...The following are comprehensive series of articles related to Pressure Relief Valves by Valve World. For thus of of you are dealing with Pressure Relief Valve design, specification, Operation, monitoring and maintenance should not missed this series of articles.

Pressure Relief Valve Types, Codes & Testing
by Lester Millard
Generally speaking, safety relief valves have been around since the 1600s in more or less the same design concept. In its primary function, the pressure safety relief valve serves to protect life and property. Acting as a 'last resort', this fully mechanical valve is designed to open based on an over pressure situation within a process pressure system, thus not only protecting life but safeguarding the investment and plant itself. This article reviews the principles of pressure safety relief valves for spring loaded and pilot operated designs. It will cover the applicable European and American codes and standards as well as end user procedures that are key elements in establishing safety and safe selection. Testing (set pressure verification) and maintenance - important criteria once the safety valve has been installed and commissioned - will also be addressed. Pressure safety relief valves should be taken very seriously. Manufactured from castings they may not look very sophisticated, but in their design, accuracy and function they resemble a delicate instrument whilst performing an essential role. Self-contained and self-operating devices, they respond to system conditions and prevent catastrophic failure when other instruments and control systems fail to adequately control process limits...

Back-Pressure effects on safety valves operating with compressible flow
by Vincenzo Dossena
The effects of back-pressures on safety valves is a potentially serious problem, but one only now being recognised by the valve industry. Research has been performed by the University of Milan, as reported in the June 2002 issue of Valve World. This report is also printed in full below. In addition, please note that RWTH's Hans-Dieter Werker has presented a paper entitled "Influence of back pressure on function and flow rate of a direct loaded safety valve" at the Valve World 2002 Conference in Maastricht.

An investigation of safety relief valve set point testing techniques
by E. Smith
In 1995/6 a BP group-wide work group met to consider various aspects of safety relief valve management and performance. One subject considered was the setting of these valves and, in particular, the use of on line set point verification (OLSPV). Traditional methods of testing such valves in BP Amoco group companies conform to the recognised industry standard API 576, and the usual procedure requires that all PSVs are removed from the plant periodically so that their condition can be evaluated in a workshop. Prior tore-installation valves are then "pop" tested on a test bench. On steam boilers the bench set pressure must also be proven in-situ by "floating" the valve. This method is both time consuming and costly. There are, however, methods of testing safety relief valves on line (with and without pressure), notably the Furmanite 'Trevitest" safety valve testing system and comparable in-situ test systems offered by e.g. Crosby and Consolidated. The benefits of these methods are lower costs and, where valves are not "spared", extended plant run times.

Safety valve noise; limits, reduction and control (PDF)
by M. D. G. Randall
What is a safety valve? How often, long and loud is its noise?
The safety valve is a device to avoid a dangerous build-up of pressure within a system that it is designed to protect. One should never forget that any redesign of the PSV system must not decrease the safety of the protected system. A safety valve is normally used with compressible fluids, whereas a relief valve is primarily used with incompressible fluids (see the introduction to Ref 1). The safety valve is generally known as a PSV and may release the process fluid directly to the atmosphere via a short stub pipe, or release the process fluid via a pipe to a flare, or some other equipment. These will be called "open vent" and "closed" PSV systems, respectively. A PSV is actuated by upstream pressure and is characterised by what is described as a "pop" action upon opening. It is important to recognise that one should not expect a gentle release of gas proportional to valve lift.

Standard Related to Pressure Relief Valve
Simple compilation of Standard Related to Pressure Relief Valve

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Saturday, January 5, 2008

Useful Documents Related to Pressure Relief Valve (PRV) - Part 1



Pressure Relief Valve (PRV) has been widely use in overpressure protection of pressure containment equipment. Regardless of vessel/column/drum/tank designed in accordance to any pressure vessel code e.g. ASME, JIS, BS, GB, etc, code will make overpressure protection by means of pressure relief device (i.e PRV, rupture disc, etc) as mandatory for fire contingencies as minimum. There are many handbooks and articles available online and FREE for read and download. Out of all, i would like to highlight a few that i think they are rather complete and you shall not miss them.

Relief Valve " What Can Go Wrong ?"
CheResources
What can go wrong in a chemical facility? Plenty! A report in the August 2000 issue of CEP1 shows that operator error or poor maintenance was the leading of cause of accidents for unfired pressure vessels eight years running. Accidents not only damage equipment but also cause injury or even death to plant personnel. To reduce the number of incidents of accidents, it is the job of the Process Engineer to analyze the process design, determine the "what can go wrong" scenario and either find a way to "design" out of it or provide protection against catastrophic failure in the event an accident does occur, i.e. install a relieving device such as a relief valve and/or rupture disk...

Relief Valve Set Pressure
CheResources
Various topics related to Process Engineering Design will be presented based on author knowledge and experiences. It covers what approaches should be taking. stress on "the correct way" without expect short cuts and rules of thumbs...

Pressure Safety Valves Design Steps
PSV Plus
A simple four design steps related to Pressure Safety Valves design process...

ANDERSON and GREENWOOD Pressure Relief Technical Manual
TYCO Flow Control
This is another Pressure Relief Valve technical manual discuss Pressure relief valve fundamentals. It is pretty good for young engineer and a refresh to experience engineer. It contents cover (1) Terminology, (2) PRV design, (3) ASME code, (4) DOT code (5) Sizing, (6) Installation, (7) Valve Types, (8) PRV Document Index, (9) Back pressure, (10) Flow Factor and (11) Flow Losses.

CROSBY'S PSV Engineering Handbook
TYCO Flow Control
The primary purpose of a pressure relief valve is protection of life and property by venting fluid from an overpressurized vessel. Information contained in this handbook applies to the overpressure protection of pressure vessels, lines and systems.

Safety Valves Related
Spirax Sarco
This website contains consolidated and fundamental informations related to Safety Valve. It covers (1) Introduction to Safety Valves, (2) Types of Safety Valves, (3) Safety Valve Selection, (4) Safety Valve Sizing, (5) Safety Valve Installation and (6) Alternative Plant Protection Devices and terminology.
Note : If you experience display problem using FIREFOX browser, please try open page with IE.

Pressure Relief Valve FAQ
FARRIS Engineering
Some common FAQ related to Pressure relief valve...
  • Can pressure relief valves be mounted horizontally?
  • How much seat leakage can I expect from a pressure relief valve?
  • How often should a pressure relief valve be serviced?
  • What are the benefits of soft seat valves versus metal seat designs?
  • When must I specify a lifting lever on a Pressure Relief Valve?
  • When must I specify the use of a Balanced Bellows pressure relief valve?
  • When should I specify a pilot operated relief valve?
Regulator and Relief Devices
Office of Pipeline Safety
This chapter contains a simplified description of the pipeline safety requirements. The complete text can be found in 49 CFR Part 192.

Calculating Relief Valves Under The New ASHRAE 15 Rules
International Institute of Ammonia Refrigeration
Between the 1994 and 2001 editions of the ASHRAE 15 standard, there were substantial changes in the method for calculating allowable length for relief discharge piping. These have confused and upset many people in the industry, including my fellow IIAR members. This short note is a simple example of how to perform calculations under the new rules.

*Continue reading at...Useful Documents Related to Pressure Relief Valve (PRV) - Part 2

*If you have any other website provide good information related to PRV, please share with us...

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Thursday, January 3, 2008

Should maximum recommended wall temperature (Tw) for carbon steel vessel used as design temperature ?


There was a interesting question raised elsewhere and i find it interesting to share with my lovely reader...
Maximum recommended wall temperature (Tw) for carbon steel vessel would be about 593 C or 1100 F as quoted in API Std 521. This value is material dependent.
Would it be accurate to say that the high "Design Temperature" could/should be used for Tw ?
My opinion would be :
There are many factors affecting fire type, heat flux, etc and wall temperature would be varies.

Heat Flux Varies
Pressure containing equipment exposing to fire, the wall temperature is very much subject to type of fire, relative distance, momentum of fire, how a fire flame impinging equipment, what type of material on fire, etc and the results is heat flux would be localized.

Low Heat Transfer
Low heat transfer between wall and vapor would leads to wall temperature far higher than the gas temperature.

Environment
Environment factor such as humidity, wind condition, etc affect the heat transmission.

As above factors are difficult to quantify, thus wall temperature of equipment would be difficult to be estimated. Personally i would always recommend to put extra efforts in fire detection, prevention and evacuation of risk instead concentrating in heat flux, wall temperature for gas expansion case. Read more HERE

However, for Pressure relief device load, i would consider to reduce the set pressure as low as reasonable possible and use the conservative approach such as taking the gas temperature at relieving condition even though it is higher than the nominated design temperature, worst F factor, etc.

It is not cost effective to consider maximum recommended wall temperature (Tw) as design temperature of the system. Otherwise 90% (if not 100%) of plant design temperature would be maximum recommended wall temperature (Tw).

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Wednesday, January 2, 2008

Consider energy saving by optimizing the pump control


Recent post "Do not under estimate pump energy cost and FREE Optimization tool for better Life cycle cost" has advised that pump operating cost is significant and shall assess and optimize during design, operation and maintenance.

There are many ways to save energy in pumping systems
  • Eliminate unnecessary uses
  • Minimize throttling
  • Assess pumping system suitability for current application.
  • Reduce pump speed or install appropriate speed control devices
  • Consider alternative pump configurations
  • Improve O&M practices
  • Improve piping configuration
Read more here by PSM.

Careful assessment on above, you may noticed that the concept behind basically originated from CAPEX, OPEX and LIFESPAN. They are inter-related. If you think around these three parameters, You may come out with more idea in energy.

One of the way to reduce energy is to provide Variable Speed Drive (VSD) motor for pump. However, combination of proper control and pump configuration design may further reduce energy consumption. There were some researches have been conducted for
  1. Throttle control
  2. Standard pump control
  3. Optimized pump control
Simple idea by optimizing the pump control can
  • save more than 45% energy comparing optimized and standard pump control
  • save more than 66% energy comparing optimized and throttling control.
Read more HERE.

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Tuesday, January 1, 2008

News related to IEM in 2008...



ANNUAL SUBSCRIPTION
REMINDER To Member of IEM :
This is just a reminder to member of IEM to pay IEM annual subscription. By right, all member (all levels) shall pay their annual subscription fees in advance on 1st Jan each year. Please refer to Fees and Annual Subscriptions and/or notice for fee structure, payment mode, transfer of grade, etc.


NEW IEM MEMBERSHIP CARD
With effect from 1st January 2008, IEM will be introducing a new membership card for all members. See below new card image.


The new card will include bar code features to facilitate CPD recording, door access, use of library services, etc in future (as planned).

REMINDER
To Member of IEM :
Please submit a “scanned” passport sized photograph (softcopy) in JPEG format and email to iemphoto@gmail.com, please indicate your name, membership number and grade. (Source HERE)

NEW IEM BUILDING
As announced earlier, IEM has acquired a NEW building and requesting Contribution/donation towards the IEM Building Fund. It is time for your action now !

Apart, members are required to contribute RM 10.00 Per Entry Per Talk as of 1st August 2007 in order to increase The Institution's Building Fund. Student Member are Exempted.

OTHER
For other general announcement, please refer HERE.


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