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How to Become a Piping Designer?

A Piping Designer is responsible for the basic design of overall pipe routing, plant layout, Overall plot plan, Unit Plot Plan, equipment layout, nozzle orientation, isometric generation, Piping MTO, developing 3D CAD models, and 2D drafting/extraction for any plant. They draft the drawings for piping and plumbing systems. For every chemical, petrochemical, power, refinery, food, and Oil & Gas industry piping designers serve an extremely important work role.

Who is a Piping Designer?

A piping designer is an engineering professional who utilizes computer-aided design and drafting systems to build and generate piping isometrics, plot plans, general arrangements, and various other drawings for construction professionals to erect the plant at the site. Piping designers are also known as drafters, draftsmen, CAD technicians, etc.

As per the Process piping Bible, ASME B31.3, a designer is a person in responsible charge of the engineering design. He assures the owner that the engineering design of piping complies with the requirements of the relevant Code (B31.3) along with any additional requirements established by the owner.

To put it simply, the Piping designer produces piping drawings and BOMs and makes use of engineering specifications such as piping material and fabrication specs, piping standard details, piping layout specifications, pipe support standards, and vendor drawings. The engineering specifications are published by the piping engineers, and the designer’s job is to make drawings in compliance with these specs. In the context of engineering projects Piping design is a collaboration between piping designers, piping engineers, process engineers, mechanical engineers, structural engineers, construction engineers, etc.

Per the ASME code, the person responsible for the design (legally liable) takes responsibility for the code compliance of the resulting design. Clearly, the piping designer is not responsible per ASME code compliance, since their job is to follow requirements given by others to produce the piping drawings. The person legally responsible for the code-compliant design is the Piping Engineer who must meet the minimum experience/qualifications set out in the ASME code. The ASME code-defined piping designer is quite different from the job title piping designers that we usually follow.

How to become a Piping Designer?

The steps for becoming a piping designer are listed below:

  • Step 1: Obtain a High School Education/ITI Certificate
  • Step 2: Obtain a Diploma in Mechanical Engineering
  • Step 3: Plant Design and Piping Engineering Course (Online or from any institute)
  • Step 4: Learn the following software:
    • AutoCAD for a 2D piping designer or Piping drafter
    • Any of PDMS, E3D, Revit, or SP3D for 3D piping designer
  • Step 5: Acquire Industry Experience: Gain working experience by working on live projects utilizing the software you learned from training institutes.

Once you get sufficient experience by working on live projects you will be able to grow your career to the next level as Senior Piping Designer, Lead Piping Designer, Principal piping designer, and so on. After an experience of at least 10 years, you will be considered a proper piping designer and can move on your career ladder to become a senior piping designer.

The process piping code ASME B31.3 has some stringent requirements for designers. As per that Code, depending on the system criticality and complexity of the job, the owner’s approval for piping designers will be required if he does not meet any one of the following four criteria:

  1. Completion of a degree, accredited by an independent agency, in engineering, science, or technology, requiring the equivalent of at least 4 years of full-time study that provides exposure to a fundamental subject matter relevant to the design of piping systems, plus a minimum of 5 years of experience in the design of related pressure piping.
  2. Professional Engineering registration, recognized by the local jurisdiction, and experience in the design of related pressure piping.
  3. Completion of an accredited engineering technician or associate’s degree, requiring the equivalent of at least 2 years of study, plus a minimum of 10 years of experience in the design of related pressure piping.
  4. Fifteen years of experience in the design of related pressure piping.

Piping Designer Jobs

An experienced piping designer is an asset for many organizations. Wherever there are piping systems to transfer or transport fluids (liquids or gases) from one place to another, piping designers are required. So, piping designers are always required for the following industries:

  • Oil & Gas (Both Offshore and Onshore)
  • Chemical
  • Petrochemical
  • Mineral
  • Food Processing
  • Steel
  • Power Generation
  • Solar Plants
  • Refinery
  • Water Sector (Water treatment plant, Sewage treatment plant, Water Desalination plant, etc)
  • Marine
  • Shipyards

Piping Designer Salary

The salary of entry-level piping designers is quite less. In India, the average salary of entry-level piping designers is in the range of 15,000 to 20,000 INR per month. However, once they gain experience and achieve the required experience their salary increases. In the mid-range (10+ years of experience), a piping designer earns in the range of 60,000-70,000 per month.

However, the salary varies from region to region. A large number of piping designers are required in the Gulf region, Singapore, Malaysia, South Korea, Norway, Europe, and the USA. In these countries, piping designers earn handsome money. In the USA, the average salary of a piping designer annually is $50,000.

Piping Design Courses

Various institutes provide online and in-person piping designer courses to help candidates learn the piping design software packages and the basics of piping design. In general, the aspirant planning to become a piping designer should learn the following basics from a piping design course:

Piping Designer Skills

The important skills that a piping designer required are:

  • CAD software knowledge (Both 2D and 3D)
  • Reading and Understanding drawings
  • Analytical skills
  • Planning skills
  • Imagination skills

What is Inconel Material? Composition, Properties, Grades, and Applications of Inconel

When thinking of materials for high performance in rigorous applications, the name of Inconel material automatically comes to mind. As the Inconel material is very expensive, the use is of limited nature. Because of this Inconel material is generally less familiar as compared to Steel or Aluminum. In this article, we will explore some basics of this unique nickel alloy.

What is Inconel?

Inconel materials are nickel-chrome-based superalloys. Inconel has high corrosion resistance, oxidation resistance, strength at high temperatures, and creep resistance. Inconel is able to withstand elevated temperatures and extremely corrosive environments.

The term “Inconel” is a registered trademark of Special Metals Corporation, USA. In 1932, the first Inconel alloy was formulated.

Composition of Inconel Alloy

The chemical composition of Inconel material varies with grade. As this is a nickel alloy, the Nickel percentage is more. Other elements present in Inconel alloy material are:

  • Chromium
  • Iron
  • Cobalt
  • Molybdenum
  • Titanium
  • Niobium

Refer to table 1 below which provides the chemical composition of some of the common Inconel material grades (Reference: https://en.wikipedia.org/wiki/Inconel). All values of elements are provided in mass %.

Inconel GradeNickel (Ni)Chromium (Cr)Iron (Fe)Molybdenum (Mo)Niobium (Nb) & Tantalum(Ta)Cobalt (Co)Manganese (Mn)Copper (Cu)Aluminum (Al)Titanium (Ti)Silicon (Si)Carbon (C)Sulphur (S)Phosphorous (P)Boron (B)
600≥7214-176-10≤1.0≤0.5≤0.5≤0.15≤0.015
61744.2–6120-24≤38-1010-15≤0.5≤0.50.8-1.5≤0.6≤0.50.05-0.15≤0.015≤0.015≤0.006
625≥5820-23≤58-103.15-4.15≤1≤0.5≤0.4≤0.4≤0.5≤0.1≤0.015≤0.015
690≥5827-317-11≤0.5≤0.5≤0.5≤0.05≤0.015
Nuclear grade 690≥5828-317-11≤0.1≤0.5≤0.5≤0.5≤0.04≤0.015
71850–5517-21Balance2.8-3.34.75-5.5≤1.0≤0.35≤0.30.2-0.80.65-1.15≤0.35≤0.08≤0.015≤0.015≤0.006
X-750≥7014-175-90.7-1.2≤1.0≤1.0≤0.50.4-1.02.25-2.75≤0.5≤0.08≤0.01
Table 1: Composition of Inconel Alloy

Properties of Inconel Material

Inconel is characterized by its ability to withstand very high temperatures. Inconel alloy maintains excellent strength even at elevated temperatures. A thick and stable protective oxide layer is formed when heated which provides excellent corrosion resistance even at high temperatures. For very high-temperature applications when steel material succumbs to creep, Inconel material is an ideal choice.

The main reason for Inconel’s very high-temperature resistance is due to the formation of an intermetallic compound Ni3Nb in the gamma double prime (ɣ’’) phase. This intermetallic phase acting as a ‘glue’ on the grain boundaries, prevents the grains from increasing in size when heated to high temperatures. Gamma prime forms small cubic crystals that inhibit slip and creep effectively at elevated temperatures.

The Mechanical and Physical properties of Inconel alloy 625 are provided below in Fig. 1:

Physical and Mechanical Properties of Inconel 625 alloy
Fig. 1: Physical and Mechanical Properties of Inconel 625 alloy

Inconel Alloy Material Grades

Inconel material has a variety of grades varying in composition and properties developed for specific applications. The common Inconel grades are as follows:

  • Inconel 188: Used widely for commercial gas turbine and aerospace applications.
  • Inconel 230: Used mainly by the power, aerospace, chemical processing, and industrial heating industries.
  • Inconel 600: Solid solution strengthened.
  • Inconel 601
  • Inconel 617: Used in ASME Boiler and Pressure Vessel Code for high-temperature nuclear applications such as molten salt reactors.
  • Inconel 625: Acid resistant, good weldability.
  • Inconel 690: For nuclear applications, and low resistivity
  • Inconel 706
  • Inconel 713C: It is a precipitation hardenable nickel-chromium base cast alloy.
  • Inconel 718: This alloy is a gamma double prime strengthened with good weldability.
  • Inconel X-750: Widely used for gas turbine components, blades, seals, and rotors.
  • Inconel 751: Increased aluminum content for improved rupture strength in the 1600 °F range.
  • Inconel 792: Added with increased aluminum content for improved high-temperature corrosion-resistant properties, used especially in gas turbines.
  • Alloy 825
  • Inconel 907
  • Inconel 909
  • Inconel 925: Inconel 925 is a nonstabilized austenitic stainless steel with low carbon content.
  • Inconel 939: Gamma prime strengthened to increase weldability.

Applications of Inconel Material

INCONEL alloy is designated as UNS N06625, Werkstoff Number 2.4856, and ISO NW6625. The NACE MR-01-75 standards list Inconel material. The Inconel material products are manufactured in all standard mill forms including rod, bar, wire, wire rod, plate, sheet, strip, shapes, pipes, tubular products, and forging stock.

The most widespread application of Inconel alloys is found in the aerospace industry. The space shuttle, Rocket engines, 3D printing technology, etc use Inconel. The nuclear industry also uses a lot of various Inconel grades. Other uses of Inconel alloys include:

  • Jet Engines
  • Fuel Nozzles
  • Engine Components
  • Afterburner Rings
  • Saltwater marine applications
  • Oil and Gas extraction
  • Industrial Processing
  • Pharmaceutical Industry

Inconel vs Monel

Both Inconel and Monel have Nickel as their primary element. However, there are many differences between the two nickel alloys. The main differences between Inconel and Monel are provided in Table 2 below:

ParameterInconelMonel
DefinitionInconel is a nickel-chromium based superalloyMonel is Nickel-copper based alloy
Maximum Nickel ContentInconel roughly has 72% nickel in the base material.Monel has around 67% nickel in the composition.
PriceInconel is more expensive than Monel.Monel is relatively cheaper than Inconel.
Elevated temperature corrosion resistance propertiesInconel has superior corrosion resistance properties at elevated temperatures.At lower temperatures, the corrosion resistance of Monel is preferred because of its low cost.
Melting Point Range2500 to 2600 Deg F2372 to 2462 Deg F
Density8.8 gm per cubic cm8.22 gm per cubic cm
HardnessHarderRelatively softer.
Temperature rangeThe maximum temperature range is 2200 Deg FThe maximum temperature range is 1000 Deg F
StrengthThe strength of Inconel is higher than Monel.Lower
Table 2: Monel vs Inconel

Butterfly Valve vs Ball Valve: Major Differences between a Ball Valve and a Butterfly Valve

When designing a system that controls the fluid flow, you’ll probably need to choose between a ball valve and a butterfly valve. Both these valves find applications in various industries, and each has its set of benefits. To choose the right product for your system, you must understand the butterfly vs ball valve features, working principles, advantages, and disadvantages.

Ball Valve vs Butterfly Valve
Fig. 1: Ball Valve vs Butterfly Valve

Understanding Ball Valves and Butterfly Valves

Ball valves and butterfly valves are considered some of the simplest control valves in the market. They are compatible with different fluid mediums and are used across a broad range of temperatures and pressure. Both valves are quarter-turn, meaning a 90-degree rotation will take the valve from fully open to fully close and vice versa. They can also be controlled manually or using electric, pneumatic and hydraulic actuators. Affordability, easy maintenance, reliability, and durability make these valves more widely accepted than the other types. Let’s look at each of these valves.

Butterfly Valve

Butterfly valves have a disc driven by a hand wheel or lever. The disc sits perpendicular to the fluid flow direction when it’s closed, while a seal sits on the valve body to ensure tight and secure closure. The stem position while opening or closing the valve is often directly proportional to the flow rate.

Butterfly Valve
Fig 2: Butterfly Valve (A) Handwheel, (B) Gearbox, (C) Stem, (D) Body, (E) Disc, (F) Seal, (G) Packing.

Butterfly valves are lightweight, have the least parts, and require little support. Similarly, they are cheaper than ball valves, especially beyond a certain diameter size. However, they aren’t suitable for high-pressure applications since high-pressure differences between the valve’s seal and the sides make it difficult to open the valve. A solution is to use a bypass valve to balance this pressure difference and enhance a smooth operation.

Since the disc interrupts fluid flow even when it’s fully open, there’s some pressure drop across the valve, limiting its ability for use in certain applications, e.g., pigging. They are also limited to ON/OFF operation and cannot be used for high-precision fluid control.

Ball Valve

Ball Valve
Fig. 3: Ball Valve (A) Handle, (B) Handle screw/Bolt, (C) Shaft, (D) Packing, (E) Seat, (F) Ball, (G) Body.

Ball valves have a hollow spherical ball held in position at one or both ends. A shaft is attached to the top end of the ball, allowing for a rotation that either opens or closes the valve. When the valve is fully open, the hole lies parallel to the fluid flow direction. The ball sits on a seat inside the valve body and can have a two-way, three-way, or four-way flow directions.

The hole in a ball valve will vary depending on the application. This hole will also feature different designs, such as a V-port and a full-port design. A V-port design guarantees stable flow control while a full port valve allows zero or near-zero pressure drop. If the bore size is less than the pipe diameter, the flow will experience some pressure drop.

Compared to butterfly valves, ball valves don’t experience leakages when fully closed. They also open easily when there’s a high differential pressure on the valve’s sides; hence do not require a bypass valve.

Advantages and Disadvantages of Butterfly Valve vs Ball Valve

While butterfly valves and ball valves have several similarities, some differences make one valve stand out in certain applications. We have rounded up the main pros and cons of both valves below.

Weight and size:

Ball valves are heavy and require significant support, while butterfly valves are lighter even at larger pipe diameters. Butterfly valves are highly recommended for applications that require larger pipe diameters (i.e., those above DN 150). The ball valve works well for size diameters below DN 50.

Leakage:

Ball valves offer a tight seal for high-pressure applications, while butterfly valves are prone to leakages at relatively high pressures.

Installation Space:

Butterfly valves have a smaller installation footprint than ball valves.

Cost:

Butterfly valves are cheaper than ball valves, especially for larger-diameter sizes.

Connection Style:

Ball valves have a wide range of connection types with flanges or threads, while butterfly valves are limited to flange style with a wafer or lug design.

Flow Control:

Ball valves are ideal for ON/OFF control and modulation purposes. It also comes with a full port valve design option that eliminates pressure drop in the valve. On the other hand, butterfly valves are only suitable for ON/OFF control, plus the valve disc restricts fluid flow, creating some pressure drop.

Butterfly Valve vs Ball Valve

The above discussions on the major differences between butterfly valves and ball valves can be provided in a tabular format as below:

ParameterButterfly ValveBall Valve
WeightButterfly Valves are Light Weight Valves. Hence, transfers less load to pipe supports.Heavy Weight is the characteristic of Ball Valves
StructureThe butterfly valve consists of a thin disk in a thin body. Simpler design.Ball valves have a sphere-like disc inside a bulky body. Complex design.
Space RequirementThe installation Space requirement of the butterfly valve is less.Ball valves need more installation space than butterfly valves.
LeakageAt high differential pressure, butterfly valves are prone to leakage.Ball valves provide a tight seal.
Flow RestrictionThe butterfly valve disc restricts the flow by creating a large pressure drop.Ball valves have less pressure drop as compared to butterfly valves.
ApplicationSuitable for ON/OFF control and proportional controlSuitable for modulating and ON/OFF Control. However, they are more used for isolation purposes.
CostButterfly valves are cheaperBall valves are expensive
ConnectionButterfly valves have a flange style with a lug or wafer designA range of connections is available for ball valves.
UsesUsed for Liquid service applicationsBall valves are capable of handling both liquid and gas.
Operating ConditionMainly used for low-temperature and pressure servicesSuitable for high temperature and pressure services
No of PortsButterfly valves can have only two portsBall valves can have more than two ports.
Table 1: Butterfly Valve vs Ball Valve

Summary

When selecting between a ball valve and a butterfly valve, you should consider all the product features, ideal use cases, and pros and cons. Understanding your system requirements and valve design expectations will also help you in decision-making.

The number of ports required, flow regulation, flow capacity, and operating conditions is the key factors to consider. You also want to choose a product from a reputed manufacturer that has a positive track record in the market. Seeking professional guidance during the selection process is highly recommended, especially if you are new to fluid control.

References and Further Studies

P-Number, F-Number, and A-Number in Welding

To ease welding procedure creation and welding procedure management, the ASME Weld Number tables provide a well-defined numbering system methodology. These numbers are assigned to the Weld base metals and filler metals. Grouping materials reduces the number of welding procedures and welder performance qualification tests for a wide range of materials. ASME Boiler and Pressure Vessel Code (ASME BPVC Section IX) has assigned a grouping scheme for base metals that consists of the P numbers and Group Numbers. Earlier there were ASME S Numbers that were removed by the code from the year 2009. Similarly, the filler metal grouping scheme consists of the F-Numbers and A-Numbers. Refer to Fig. 1, which clarifies what these numbers relate to.

P-Number, F-Number, and A-Number in Welding
Fig. 1: P-Number, F-Number, and A-Number in Welding

What is the P Number in Welding?

Depending on the material characteristics like composition, weldability, brazeability, design consideration, heat treatment, and mechanical properties, ASME BPVC assigned P-Numbers to the base metals. The code assigned the same P-number for the materials with similar material characteristics. These are listed in Table QW/QB-422 of ASME. While changing the base metal from a qualified WPS to a new base metal, requalification or a new PQR is not required if the new base metal falls in the same P-Number.

These base metals are grouped by material and the assigned P-Numbers are constant for that specific material group. For example, the base metals of Low Carbon Steel or Carbon Manganese material fall in P-Number 1. The following table (Table-1) provides the P-number ranges for various metals and alloys.

Sr. No.Type of  Steel, Metal, AlloyP-Number
1.Carbon Steel (C-Mn )1
2.Low Alloy Steel (Cr-Mo Steels)4, 5A, 5B, 5C, 15E
3.Stainless  Steels (Cr-Ni steels)8, 10H
4.Nickel & Ni-base alloys41 to 49
5.Aluminum & Aluminum alloys21 to 26
6.Copper & copper alloys31 to 35
7.Titanium & titanium alloys51 to 53
8.Zirconium & zirconium alloys61 and 62
Table 1: ASME P-Number Table

From the ASME Sec IX table, QW/QB-422 can find the P-number of a specific grade of material, i.e. which material falls under which P-number and what is product form i.e. plate, forging, sheets, fittings, etc.

P-number is generally mentioned in WPS & PQR for procedure qualification and in WPQ for performance qualification.

What is the F-Number in Welding?

As the name suggests, F stands for Filler number. Depending on the composition, the microstructure of the material F-number is assigned to welding consumables i.e. filler wires, and electrodes to reduce the procedure and performance qualifications. F-number is generally mentioned in WPS & PQR for procedure qualification and in WPQ for performance qualification. The ASME Sec IX (QW-432 assigned the F-number on the basis of type of consumable, usability of consumable, metallurgical compatibility, heat treatment, and other mechanical properties. The same F no is assigned to carbon steel as well as stainless steel filler wires. For example. ER70S-6 & ER308 have the same F no. i.e. F no. 6. The following table (Table-2) provides the F-number ranges for various consumables as classified in ASME Section.

Sr. No.Type of  Steel consumablesF-Number
1.Carbon Steel1 to 6
2.Low Alloy Steel (Cr-Mo Steels)1 to 6
3.Stainless  Steels (Cr-Ni steels)5, 6
4.Nickel & Ni-base alloys41 to 46
5.Aluminum & Aluminium alloys21 to 26
6.Copper & copper alloys31 to 37
7.Titanium & titanium alloys51 to 56
8.Zirconium & zirconium alloys61
9.Hard-facing weld metal overlays71 and 72
Table 2: ASME F-Number Chart

From the ASME Sec IX, table QW-432 can find the F-number of specific consumables classified as per ASME Sec IIC. With the F-number there is a reduction of procedure and performance qualification as the same F-number of material does not require requalification.

From the ASME Sec IX, table QW-433 can be referred to for the welder performance qualification range. A snapshot is given below:

What is the A-Number in Welding?

As from the name, A stands for analysis. A-number is designated by ASME to weld metal deposition composition analysis to reduce the number of procedure qualifications in Welding. From the ASME Sec IX table QW-442 can be referred to for different A  number is given to different groups of metals/alloys. A-number is generally mentioned in WPS & PQR. It is not essential for performance qualification i.e. not mentioned in WPQ.

Note that the A-Number gives the chemical composition of the weld metal in the “as-welded” state, not of the filler metal product in its raw form.

Click here to learn Welding Technology in detail.

Video Courses in Welding

To learn more about welding the following video courses you can refer to:

What is Nitrogen Purging? Applications, Procedures, and Benefits of N2 Purging

Nitrogen purging plays an important role in the safety and functioning of various plants that are susceptible to fire hazards. In fire and explosion protection engineering, an inert (ie, non-flammable) purge gas (like nitrogen, helium, argon, etc) is introduced into an enclosed system (eg, a container or process vessel) to prevent the formation of a fuming flammable atmosphere. This inert gas helps to mitigate the risk by overriding hazardous fire/explosion-forming agents like oxygen. In this article, we will explore more about Nitrogen purging, Its definition, procedure, benefits, etc.

What is Nitrogen Purging?

Many a time people in safety engineering ask what nitrogen purging actually means. Nitrogen purging is the process of introducing nitrogen into closed vessels, pipelines, containers, etc to displace undesirable hazardous atmospheres and to clean the inner walls. Nitrogen in the nitrogen purging process pushes out oxygen and moisture and creates a stable non-combustible environment, thus reducing the potential hazard.

Why Nitrogen Purging is Required?

Chemical Industries like acetylene production plants, Oil and Gas plants require nitrogen purging on a regular basis. The main benefits that nitrogen purging provides are:

  • Nitrogen purging helps in removing the oxygen % from the internal surfaces of the pipelines and equipment. So, the possibilities of sparks and fires are greatly reduced during operation.
  • Nitrogen purging removes moisture that may be present which helps in lowering the dew point.
  • The nitrogen purging process ensures a safe environment for the workers and nearby residents.
  • It prevents chemical alteration of the product.

Uses of Nitrogen Purging System

A lot of industrial manufacturing processes use nitrogen purging to eliminate moisture or oxygen-rich air. Introgen purging equipment is sometimes integrated with oxygen-sensitive operations to avoid unfavorable conditions. Major industrial applications of the nitrogen purging process are:

  • Transformers and other volatile electrical environments enhance safety by using the N2 purging procedure.
  • Nitrogen purging in the brewery industry extends the shelf life of beer.
  • Ships and tankers use nitrogen blanketing to remove potentially combustible environments.
  • Organic compounds generating chemical and petrochemical industries widely use nitrogen purging processes to eliminate toxic gases from process chambers.
  • Atmosphere Packaging and Food industries apply the nitrogen purging process to remove moisture, oxygen, and other gaseous impurities.
  • Nitrogen purging is widely used in oil and gas pipeline projects for drying, cleaning, and limiting oxygen concentrations.
  • To eliminate compounds affecting weld quality, metal fabrication industries use N2 purging systems.

Why Is Nitrogen Used for Purging?

Nitrogen is dry, non-combustible, and economical as compared to other inert gases. This makes the nitrogen purging process more affordable.

Difference between Nitrogen Purging and Inerting?

The purge gas is inert. By definition, it is non-flammable, or more precisely, non-reactive. The most common purge gases available commercially in large quantities are nitrogen and carbon dioxide. Other inert gases, eg. Argon or helium can be used. Nitrogen and carbon dioxide are not suitable for purge applications in some cases because these gases can chemically react with fine dust from certain light metals.

Since an inert purge gas is used, the purge procedure can (erroneously) be called inerting in everyday language. This confusion can lead to dangerous situations. Carbon dioxide can be considered a safe, inert purge gas. Carbon dioxide is an inert gas that is not safe for inactivation as it can ignite vapors and cause an explosion.

Difference between nitrogen purging procedures from other industrial explosion prevention methods?

Fires and explosions can also be prevented by controlling ignition sources. However, purging with an inert gas (nitrogen) provides a higher level of safety because it is guaranteed that no flammable mixture is formed. Therefore, it can be said that primary prevention is relied on to reduce the possibility of a spreading explosion, and ignition source control relies on secondary prevention to reduce the possibility of an explosion. Primary prevention is also referred to as essential safety.

Types of Nitrogen Purging Procedures

There are four main industrial nitrogen purging procedures that are widely used. They are:

  1. Displacement purging (Plug effect)
  2. Dilution Purging
  3. Pressure swing Purging, and
  4. Vacuum purging

Displacement purging (Plug effect)

In a displacement purge, an inert gas is injected into an open vessel to evacuate hazardous or noxious gases. Slow flow is maintained (velocity < 10 m/s).  

Displacement Purging Process Configuration
Fig. 1: Displacement Purging Process Configuration

The displacement nitrogen purging procedure is mainly used for high H/D (height/diameter) ratios. Ideally, the inert gas should be denser than the displaced gas on Fig. 1 shows how nitrogen is used for the displacement purge of the vessel. Gas is transported in tankers. Liquid nitrogen is vaporized in the vaporizer and gaseous nitrogen is injected into the vessel. Nitrogen pushes the atmosphere out of the vessel through an outgassing valve. The amount of nitrogen required is relatively small, typically 1.2 times the capacity of the vessel.

Dilution Purging:

A dilution purge involves introducing an inert gas to reduce the concentration of hazardous gas.

Dilution Purging Process Configuration
Fig. 2: Dilution Purging Process Configuration

The dilution nitrogen purging procedure is used when the H/D ratio of the machine is low. The amount of nitrogen required is approximately 3.5 times the capacity of the vessel. The configuration in Fig. 2 shows how nitrogen gas is vaporized and injected into the device with the outlet valve open. The diluent gas, which consists of noxious gases and nitrogen, is released into the atmosphere or further processed.

The following  equations can be used for this process:

The number of volume changes:                               i = ln [Ca ⁄ Ce]

The Volume of inert gas required:                              VN = i · VB   

Here,

  • i = Volume change
  • Ca = Initial concentration
  • Ce = Final concentration
  • VN = Volume of inert gas
  • VB = Volume of vessel

Pressure swing Purging:

In pressure swing purging, the closed device is sprayed with an inert gas. When the gas is released, the dangerous or harmful gas disappears. The process (closed-injection-open-exhaust) continues until the desired concentration of harmful gases in the device is reached. Variable pressure purge is used, for example, when the inlet and outlet are close to each other. The device must also be a pressure vessel. In the pumping pressure, there is a difference between vacuum purification and excessive production. One of the main goals of the pressure swing occurs due to hazardous substances or harmful substances, such as oxygen. The residual concentration of harmful substances can be calculated in the following formula:

CSR=(P1/P2)n * (CSG-CSI) +CSI

Here,

  • CSR = hazardous substances residual concentration
  • CSG = Concentration of hazardous substances in mixtures
  • CSI = Concentration of hazardous substances in inert gas
  • n = Number of pressure swings
  • P1 = Pressure 1 (before inerting)
  • P2 = Pressure 2 (after inerting)

Vacuum purging

Vacuum purge involves the use of a vacuum pump to remove harmful gases and then supply inert gas to the evacuated unit. This process is repeated until the desired hazardous gas concentration is reached. Vacuum purge is particularly suitable for machines with multiple dead zones.

The effective inert gas requirement  is calculated as follows:

VN = VB * f * n

Here,

  • VN = Inert gas requirement in m³ 
  • VB = Vessel volume in m³
  • f = Pressure change ratio
  • n = Number of pressure swings

The pressure change ratio equation is as below:

f=1-(P1/P2) (P1/P2)<1

Here,

  • f = Pressure change ratio
  • P1 = Pressure before inerting
  • P2 = Pressure following inerting

Nitrogen Purging in Pipelines

Newly laid pipeline network and sometimes after maintenance and shutdown work nitrogen purging in pipelines is performed. This process is important to remove retained moisture, oxygen, and other impurities that may otherwise change the quality of the fluid being transported.

Nitrogen purging in pipelines is a pretty straightforward procedure. Pressurized nitrogen gas is forced through pipelines that force out all gaseous and particulate impurities present inside. However, Pipeline nitrogen purging may sometimes involve risks. Hence, To safely conduct the pipeline nitrogen purging process, the operators should take the following steps:

  • Ensure proper instruments/apparatus handling
  • The operation must be performed by trained personnel.
  • Emergency protocols for shutdown and personnel evacuation must be well informed to all.
  • Personal protective equipment must be worn by all personnel involved in purging operations

What is Inerting? Gases Used for Inerting and Their Selection Criteria

Inerting refers to the process of introducing an inert gas into an enclosed space to release the gas already present, resulting in a kind of hazard. Although this process can be used to displace toxic gases, it is most commonly used to displace oxygen or to reduce the oxygen concentration in a space when the space is completely enclosed and substitution is not possible.

An inerting system reduces the combustion potential of flammable materials that are stored in a confined space. A common example of such a system is a combustible liquid-filled fuel tank that transports gasoline, diesel fuel, jet fuel, aviation fuel, or rocket propellant. Once the fuel tank is filled and during use, a space vapor barrier above the fuel known as the ullage is created. It contains evaporated fuel mixed with air containing oxygen, the important element necessary for combustion. An inerting system is used to replace the air with inert gas, such as nitrogen, argon, helium, etc. to avoid the combustion hazard.

Reason for Inerting

There are many chemical processes where inerting is required

  • to make the system or process explosion-proof
  • to eliminate unwanted reactions 
  • to keep food away from moisture 
  • to ensure safety during maintenance work. 

Engineers often rely on inert gases and specialized inert equipment, as these goals cannot always be achieved by technology and equipment design alone. There are many situations where deactivation is the only way to meet safety standards during the production process and maintenance. In other cases, inerting is used to improve product quality.

Basic Principle of Inerting

The basic principle of inerting is to completely or partially replace air containing oxygen and flammable and/or toxic gases that often contain moisture or inert gases.

Inerting is based on the principle that a combustible (or combustible) gas can only burn (explode) when mixed with air in the correct proportions. The flammability limit of the gas determines this ratio, i.e. the flammability range. In terms of combustion technology, it can be said that the inert gas inlet dilutes the oxygen below the limiting oxygen concentration. Inerting prevents the formation of a flammable mixture that spreads by definition. Inerting introduces an inert gas to make the flammable mixture safe.

Gases Used for Inerting

The most widely used gases for inerting are Nitrogen and Carbon dioxide. Other gases such as argon and helium are applied in certain instances. Steam and exhaust gases are used in some industrial applications.

Selecting the Inert Gas

There are various criteria that influence inert gas selection. Some of these are:

Dangers of fire and explosion and/or their effects or actions 

Nitrogen and carbon dioxide are not completely inert, but they are the best gases at room temperature. At high temperatures, nitrogen reacts with very few substances such as lithium, which forms lithium nitride. 

6 Li + N2 → 2 Li3N

Nitrogen can react with magnesium, Silicon at temperatures between 400 ° C and 1800 ° C for nitriding, titanium, and other metals:

2 Ti + N2 → 2 TiN

The reaction with oxygen occurs only at very high temperatures. In comparison, carbon dioxide reacts with a longer list of substances containing strong bases. Amine, anhydrous ammonia, lithium, potassium, sodium, magnesium, beryllium, aluminum, chromium, manganese, titanium, uranium, and acrolein. The decomposition temperature of Carbon dioxide is 2000° C, but this is rarely a problem. However, increasing the pressure increases the solubility of this gas.

Effect on product and exhaust gas

When steam is used for inactivation, the condensate produced can sometimes be hazardous. inactivation. When shipping, readily available exhaust gases are used in the oil tank, so the fuel-to-air ratio must be carefully controlled. 

Cost

Inert gases are generally too expensive to use for inertization and are not as effective as inert gases. nitrogen. However, they are often used to inactivate light metal dust. For example,  Aluminium dust explosions can be prevented by using argon and that is why it is used in fire extinguishing systems for such explosions. 

Specific heat capacity of inert gas

 The specific heat capacity of a given inert gas determines its effectiveness. The higher the specific heat capacity, the higher the inert efficiency. Table 1 shows the corresponding values.

Inerting AgentSpecific Heat* (Btu/(lb mole/0F)Specific heat* (kJ/kmol/K)
Nitrogen729.308
Carbon Dioxide8.836.844
Helium520.934
Argon520.934
Steam1771.176
Table 1: Specific Heat of Selected inerting agents at 00C and at constant pressure (* Values at constant pressure, steam at 270C, other values at 00C)

The reason for this is that diluting with a high specific heat inert gas reduces the areas at risk of ignition. According to this logic, carbon dioxide is again favored over nitrogen because less inert gas is required.

Molecular structure of inert gas

The molecular structure of an inert gas directly affects its efficiency. Carbon dioxide is a triatomic molecule, nitrogen is a diatomic molecule, argon, and helium are monoatomic molecules. Polyatomic molecules can absorb more energy because they contain more free molecular vibrations. Therefore, the inert effect decreases in the following order:

CO2 → N2 → He, Ar

Figure 1 shows the effectiveness level of the inactivating agent, using the flammability of methane as an example.

Influence of Various inerting agents on the flammability of methane
Fig. 1: Influence of Various inerting agents on the flammability of methane

The density of inert gas

Density also plays a particularly important role. If the density of the Inactive gas is greater than the density of the replacement gas, the free space above the Inert gas injection point may not be deactivated.

Table 2 shows a comparison of the density of the selected gas to that of air.

Types of GasDensity in Kg/m3 at 1013 m-bar and 00CDensity relative to Air
Air1.2931
Nitrogen1.25050.967
Hydrogen0.08990.0696
Argon1.78371.38
Oxygen1.4291.105
Carbon dioxide1.97671.529
Table 2: Density of selected gases and their densities relative to air

Application of Inerting in Chemical Industries

The chemical industry uses a wide range of materials, technologies, and devices. Inactivation or inerting is especially used for: 

  • Reactor, Mixer 
  • Centrifuge and vacuum filter 
  • Wheat mixing plant 
  • Tank farms, ships 
  • Dryer, silo 
  • Gas station 
  • Oil line and fuel line 
  • Industrial service

Objectives of Inerting Activities

The predominant objectives of those inerting activities are to

  • Prevent explosive atmospheres from forming in equipment along with reactors
  • Ensure secure begin-up and shutdown of flora and equipment 
  • Avoid explosion dangers in the course of garage and delivery of flammable substances
  • Protect merchandise in opposition to atmospheric oxygen whilst oxidation reactions might impair  fine 
  • Protect in opposition to atmospheric moisture, both to keep product fine or to make sure optimum  downstream processing, as an example in grinding
  • Prevent fitness and protection risks in the course of the renovation of flora, equipment, and pipelines.

Different Modes of Inerting Application

Continuous Applications:

  • Protection of the production process to prevent fire, explosion, and oxidation (for quality assurance) 
  • Inert solvent containers and transport equipment to prevent fire and explosion

Intermittent applications:

  • Purge pipeline
  • Tank purging
  • Deactivation of the filter system
  • Inactivation of silos
  • Deactivation of grinding equipment
  • Smoke evolution in the mine

Types of Inerting

Depending on the application, inerting can be classified into two groups as mentioned below:

Partial inerting:

The oxygen concentration is reduced to a level low enough that the mixture will no longer explode.  In the case of partial inertia, the goal is to reduce the oxygen concentration in the mixture to a level where it will no longer explode.

Complete inerting:

Complete inertia involves increasing the ratio of inert gas to a combustible material to a level at which the addition of any amount of air cannot produce an explosive mixture.