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What is Smart Plant Instrumentation (SPI) Intools?

SmartPlant Instrumentation (SPI) is one of the foremost instrumentation engineering tools developed by Intergraph. Earlier, the same software was well-known as the Intools. The software acts as a single and widely used instrumentation application that is used in Engineering, Procurement, and Construction (EPC) Projects. Smart plant instrumentation helps in accessing and updating the instruments used in any plant for various tasks.

The software is used for managing and designing various activities including:

  • Instrumentation management,
  • Generation of instrumentation data sheet,
  • Control valve and orifice plate sizing,
  • Generating Loop diagram
  • Programmable Logic Controller (PLC) wiring,
  • Creating Hook-up drawings,
  • PLC-DCS I/O assignment, etc

The majority of EPC firms use this instrumentation design tool. Smartplant instrumentation creates a single engineering design environment that creates and manages data required by instrumentation engineers. This software is an all-in-one solution for all Instrumentation and Process deliverables. The software package can seamlessly manage those data consistently throughout the design lifecycle.

What’s inside SPI and how does it work?

Project execution involves several tasks, to which many disciplines contribute. Executing these tasks in a systematic way makes the engineering deliverables better which will support the plant construction and operations.

SmartPlant Instrumentation is a platform that is progressing toward a module-oriented environment. This indicates this interface deals with the script at hand, for example:

Process module – Collect process data from SmartPlant P&ID. Edit information and add that data set into the instrument design basis wherever applicable.

Instrument Index module – Recall and expand the rule base instrument design basis from the P&ID into all physical instruments. This function performs as Process – Instrumentation synchronization.

Specification module – By using Engineering Data Editor create specific interfaces as well as user experiences that can be configured to perform the specific task – for example, to create instrument datasheets/specifications, which include SmartPlant Instrumentation data along with the data those are related to or coming from vendors specifications.

Wiring module – Build up the Engineering Data Editor for junction boxes, marshaling cabinet (including DCS and PLC), assigning the cable and wiring data script to auto-connect instruments with junction boxes, and junction boxes with cabinets. This task includes a loops check for connectivity. Here comes Instrumentation – Electrical synchronization.

This extended focus increased productivity and asset management quality.

How does Intergraph Data sharing work on SPI?

SmartPlant Instrumentation acts as a receiving engine from various data sources, which includes the process group, piping department, and electrical and instrumentation team. The outcome data then feeds into the piping group for the equipment or inline instruments, and interlocks for electrical, in addition to interfacing and interacting with vendor and third parties catalogs.

SmartPlant Instrumentation also supports operational activities, not only generating new and even as-built data also. SPI also offers a seamless interface for calibration with Fluke, and for maintenance scheduling interface with ERP providers such as the SAP platform.

Vendor data and catalog access are rapidly becoming more important to drive productivity and engineering design quality. Instead of finding and re-typing in SPI, you can easily access vendor data, for example, I/O card details for DCS, instruments under vendors’ scope like E+H, or valves from Rosemount/Emerson. SmartPlant Instrumentation makes it easy to get accurate data quickly.

How SmartPlant Instrumentation (SPI) contributes to the plant life cycle?

SmartPlant Instrumentation gains value for instrument-related workflow throughout the life cycle of the plant. SPI contributes to Engineering and Design, Procurement, Construction, Commissioning, Operations, and Maintenance.

Engineering and Design  –  SmartPlant Instrumentation helps to manage and create instrumentation data in a discrete database, which facilitates faster, synchronal engineering to reduce project manhours and cost. This software assures data accuracy, persistent deliverables, effective and optimized change management system. By creating various engineering rules this software maintains data integrity. Vast two-way integration with other software (like AutoCAD, Microstation, etc.) even with vendors (like Yokogawa, Emerson, etc.) to reduce manual entry and design time. Quality of data increases.

Procurement  –  Design data can easily be transferred from SmartPlant Instrumentation to Intergraph’s SmartPlant Materials, which can shorten the procurement cycle. Warehouses can easily maintain the purchase and change-over records in SmartPlant Materials, which makes procurement hassle-free.

Construction  – The user can extract control panel drawing from the database. The contractor can start construction for the control panel and can modify it whenever required by simply modifying the database.

Commissioning  –  With the help of SmartPlant Explorer along with SmartPlant Instrumentation users can access data and test loop continuity. SmartPlant Explorer is more towards mark-up capability via the online Web.

 Operations and Maintenance  –  SmartPlant Instrumentation along with SmartPlant P&ID acts as a single data package. The operator can easily access P&ID and instrument data simultaneously while operating the plant. These data are consistent, accurate, and current. So there is less chance of error, which makes maintenance easy.

Advantages of Smart Plant Instrumentation (SPI)

Plant engineers and operators use Smart Instrumentation Intools for asset performance management which translates to a variety of functions like power management, process automation, maintenance systems, safety, and asset optimization. The Intools software makes the sensors, electronics, and process diagnostics data to be centralized and aligned with tasks. This result in huge saving in labor hours and cost with improved compliance and consistency in managing change.

The major benefits that Smart instrumentation software packages provide are:

  • Reduced Risk, downtime, and increased profit.
  • Fully automated generation of engineering deliverables like wiring diagrams, loop diagrams, and specifications from centralized data.
  • Improved performance of control system and associated documents.
  • Rapid execution with custom design rules
  • Improved work efficiency
  • Reduced cost due to data leveraging and consistent design.

How SmartPlant Instrumentation gain value?

SmartPlant Instrumentation can easily facilitate small to very large projects. With a single source of all data offered, this software ensures that consistent changes are reflected, recorded, and flagged. This software platform helps to reduce project cycle manhours and gain value.

Intergraph calculated after facilitating a Large LNG project like 18 billion US$ in SmartPlant Instrumentation can save up to 40% of the project cycle manhours. Refer to the following figure

Reduction in Man-hour Cost when using SPI
Fig. 1: Reduction in Project Man-hour Cost when using SPI Tools

What is API 5L Pipe? Its Grades, Specification, and Schedule chart

API 5L is a seamless and welded carbon steel pipe material specification. API 5L pipes are widely used to transport oil, water, and gases in the pipeline industry. Depending on the strength, schedule, and service requirements API 5L pipes are manufactured in various grades and are suitable for both onshore and offshore applications. In this article, we will learn about the various grades, specifications, and schedule charts of API 5L pipes.

API 5L pipes in the oil and gas, water, and petrochemical industries are available in two Product Specification Levels (PSL) depending on quality levels. The first one is PSL1 which provides a standard quality level. The other one PSL2 provides additional mandatory requirements in strength, chemical composition, NDT, or notch toughness.

Grades of API 5L Pipes

API 5L pipes are produced in various grades. Each API 5L grade varies in its strength capabilities. A unique alpha or alphanumeric designation is assigned to each grade of API 5l pipes. Leaving Grade A and Grade B, all other API 5l grades mention the specified minimum yield strength in their numerical portion of the designation. These yield strength values are expressed in KSI (kilopound per square inch) for the USC unit and in MPa (Mega Pascal) for the SI unit system.

The common grades of API 5L pipes that are widely used are:

  • API 5L Grade B (USC unit system) or L245 (SI unit system)
  • API 5L Grade X42 or L290
  • API 5L Grade X52 or L360
  • API 5L Grade X60 or L415

Other API 5L grades that are also manufactured for various applications are:

  • API 5L Grade A25 or L175
  • API 5L Grade A25P or L175P
  • API 5L Grade A or L210
  • API 5L Grade X46 or L320
  • API 5L Grade X56 or L390
  • API 5L Grade X65 or L450
  • API 5L Grade X75 or L485

Various letters have suffixed these grades to indicate special requirements like N denotes normalized, Q denotes quenched and tempered, and M denotes thermomechanical rolled or formed.

As informed earlier the numerical value denotes the specified minimum yield strength in USC or SI unit. For example, for API 5L X42 material the term 42 denoted 42KSI as the specified minimum yield strength of the material. Similarly, API 5L L360 denotes the specified minimum yield strength for the material is 360 MPa.

Purchasing Information

While purchasing the API 5L material the following details must be specified in the purchase order or material data sheet.

  • PSL levels (PSL1 or PSL2).
  • Grade of the Pipe required (Proper pipe designation).
  • Pipe Size, Outer diameter, and thickness.
  • Random or Approximate length.
  • Seamless or Welded.
  • Quantity of pipe required (Total length or Total mass).
  • Pipe end connection.
  • Coating and lining requirements.
  • Fluid service sour or sweet.
  • Any marking requirements.
  • Any special requirements, etc

Specification of API 5L Pipe

API 5L Pipe specification is prepared with respect to various aspects as listed below:

Standard Scope: The scope of API 5L pipe mainly includes the application of the pipe for water and oil and gas pipeline transmission.

Manufacturing types: The specification includes the manufacturing types as welded and seamless. Cast pipes are not covered in the specification.

Pipes under 24″ are usually seamless or ERW, whereas large diameter pipes are SAW/DSAW. LSAW is used up to 48″ in size whereas SSAW/HSAW can be used up to 100″ in size.

Different Grades: API 5L line pipe specification covers Gr. A, B, X42, X46, X52, X56, X60, X65, X70, X80, etc. There are various delivery conditions as required for different applications.

Material specifications (Chemical and Mechanical): The material datasheet specifies the chemical composition and mechanical properties of each grade of API 5L pipe material.

Test Methods: Hydrostatic test is the most common testing method applied for the API 5L line pipe to investigate joint leakage. Other tests include the bend test, flattening test, etc. The line pipe must be free from cracks, sweat, leaks, or any other defects.

Other important considerations are:

  • Tolerances on pipe diameters, wall thickness, out-of-roundness
  • Common defects
  • Line pipe history and milestones
  • Applications
  • Pipe designation
  • Carbon equivalent limits
  • Jointer welds
  • Ends type: plain, beveled, threaded ends
  • Repairs Requirements
  • Pipe markings and end colors
  • CVN impact test
  • DWT test
  • Hardness test

API 5L Schedule Chart

Similar to other carbon steel pipes, the pipe thicknesses are not standardized for all API 5L pipe grades. The OD of pipes matches the OD of other carbon steel pipes. However, the thickness varies. Depending on high strength the thickness used for specific applications is usually reduced. High-strength and low-thickness pipelines are widely used in the pipeline industry.

Manufacturers of API 5L pipes provide their schedule chart mentioning the available pipe thicknesses with respect to pipe size. The weights and prices per unit length are also usually provided in the API 5L pipe schedule chart. Some grades of pipe schedules like API 5L grade pipes have standardized pipe schedules similar to as provided in ASME B36.10. But for high-strength line pipes, for example, X60, X52, X42, etc have standardized as well as non-standardized pipe schedules.

A typical API 5L standardized pipe schedule chart is provided in Fig. 1 below.

API 5L Standardized Pipe Schedule Chart
Fig. 1: API 5L Standardized Pipe Schedule Chart

What is a Chemical Injection Quill? Types, Configurations, Applications

The injection quill is a precision-engineered mechanical device. As this device is widely used in the chemical injection process it is popularly known as the chemical injection quill. Various chemical industries use injection quills to provide an effective and safe means of injecting liquid chemicals into a vessel or pipeline system. They are usually a part of metering systems.

Applications of Chemical Injection Quills

Injection quills dose the chemical into the interior section of the flow and thereby keeping the chemical away from the sidewall and fittings. Chemical injection quills serve as an interface between the chemical feed line and the processing pipeline. The quill delivers the chemical efficiently into the interior of a process pipeline flow. Various chemical industries make use of chemical injection quills in applications like additive injection, bio-treatment, chemical injection, removal and separation processes, etc.

Chemical injection quills are used in a wide range of industries and processes, including:

  • Water Treatment: In water treatment applications, chemical injection quills are used to introduce chemicals such as chlorine, chlorine dioxide, coagulants, and pH adjusters into the water to disinfect it, remove impurities, and maintain the desired water quality.
  • Oil and Gas Industry: Chemical injection quills are employed in the oil and gas sector to introduce chemicals that aid in pipeline maintenance, inhibit corrosion, prevent scale formation, and enhance oil recovery during production.
  • Chemical Manufacturing: In chemical production processes, quills are utilized to introduce catalysts, reactants, and additives into reaction vessels for precise control of chemical reactions.
  • Pharmaceuticals: Chemical injection quills play a role in pharmaceutical manufacturing by accurately introducing active pharmaceutical ingredients (APIs) and other substances during drug synthesis.
  • Wastewater Treatment: In wastewater treatment plants, chemical injection quills are used to introduce chemicals for flocculation and coagulation, aiding in the removal of suspended particles and pollutants.

Types of Chemical Injection Quills

To meet the demand for handling various chemical substances, there are a wide variety of injection quills that are found in industrial applications. All these chemical injection quills are categorized into one of the following two types:

Retractable Quills allow the operator to retract the injection quill without fully depressurizing the vessel or pipeline. These types of injection quills are complex in design and highly beneficial for clog-prone systems requiring frequent maintenance but where frequent shutdown is not feasible.

All retractable injection quills have the following components:

  • Solution Tube that carries the treatment chemical.
  • Restraint system to keep the solution tube in place.
  • Isolation valve assembly consists of a valve and compression gland.

Non-Retractable Quills where the vessel or pipeline must be depressurized to remove the chemical injection quill. Non-retractable types of injection quills are widely used for chemical systems that do not form frequent deposits to clog the quill.

Retractable vs Non-retractable Injection Quills
Fig. 1: Retractable vs Non-retractable Injection Quills

Depending on the number of Ports, injection quills are classified as follows:

  • Dual Port Injection Quill: These types provide a uniform and rapid dispersal of two chemicals injected into one port.
  • 3-port Injection Quill: Deaerators, boilers feed water tanks, etc use this type of injection quill for more uniform and rapid dispersal of chemicals into the center of the process pipe.
  • 4-port Injection Quills: These are specially designed injection quills to disperse four chemicals into one port.

Chemical Injection Quill Configurations

Industrial injection quills are manufactured in various configurations, connections, and fittings. The configuration varies from a simple fabricated tube/probe to an integrated assembly with isolation valves and non-return valves. A compact integrated assembly consisting of the chemical injection quill, probe, double block & bleed assembly, and an integral non-return check valve is always beneficial.

Injection quills can be used as sampling quills by redesigning the probe and removing the integral check valve to safely take out fluid samples from the process line.

Chemical injection quills are mounted into the pipeline through a fitting. The probe is inserted and extended to the center of the process line. The other end of the injection quill connects to the chemical feed line by a pipe or tubing connection.

Designing An Injection Quill

The design of an injection quill is governed by various parameters like:

Design calculation

The wake frequency is calculated following the guidelines provided in the ASME PTC 19.3 TW standard for Thermowell as the injection quill is similar to it. The design of chemical injection quills needs both thermal and stress considerations. So process parameters like fluid, temperature, pressure, velocity, flow rate, density, viscosity, etc must be known for designing the injection quill.

Material of Construction

The material grade of the injection quill is selected such that the material is suitable for the service and the chemical to be injected. As the quill forms an integrated assembly together with the DBB and the check valve, several parameters similar to an isolation valve design must be evaluated.

Dimensions

The length of the injection quill is one of the most important parameters for wake frequency calculation. The length can be customized. Bore Size, Insertion Length, Tip Diameter, Root Diameter, Overall length, etc are the important dimensions to be considered during design.

Nozzles

In general, cylindrical tubes or nozzles are used for injection quills. However, specially designed nozzles depending on the application can be designed.

Mounting options

The design of injection quills can vary based on mounting options. Various different mounting options like flanged, welded, or threaded are possible. However, the quill/probe outside diameter (O.D.) must fit all the way down to the process stream.

Working Principle of Chemical Injection Quills

When the chemical injection pump operates, it pushes the chemical through the quill, which has a small orifice or series of holes at its tip. As the chemical is released into the fluid stream, it undergoes turbulent mixing with the surrounding fluid, promoting rapid dispersion and integration. The quill’s design helps prevent direct contact between the chemical and the pipe walls, which could lead to unwanted reactions or buildup.

Components of a Chemical Injection Quill Assembly

A chemical injection quill assembly consists of several essential components that work together to introduce chemicals or substances into a fluid stream. The specific design and configuration of the assembly may vary depending on the application and the requirements of the system. Below are the main parts commonly found in a chemical injection quill assembly:

  • Injection Quill Body: The injection quill body is the main component of the assembly, usually a hollow tube or pipe made from materials compatible with the chemical being injected and the fluid in the system. It connects to the chemical injection system, such as a pump or storage tank, at one end.
  • Injection Orifice or Holes: At the tip of the injection quill, there is an injection orifice or a series of small holes. These openings are responsible for releasing the chemical into the fluid stream. The size and number of orifices or holes are critical to achieving the desired injection rate and dispersion.
  • Flange or Connection End: The end of the injection quill assembly that enters the fluid stream is typically flanged or threaded for easy installation and connection to the process piping. The type of connection used depends on the specific requirements of the system.
  • Flange Gasket: A flange gasket is placed between the flange on the quill and the process pipe to create a secure and leak-free connection. The gasket material is chosen to be compatible with the fluid and the chemical being injected.
  • Supports or Holders: Depending on the installation and process conditions, the injection quill may be supported by holders or brackets to keep it stable and properly positioned in the fluid stream.
  • Injection Tube Extension: In some applications, a tube extension or extension pipe is attached to the injection quill to ensure that the chemical is introduced at the optimal location within the fluid stream. This extension can vary in length depending on the specific requirements of the process.
  • Ball Check Valve (Optional): Some chemical injection quill assemblies may include a ball check valve to prevent the backflow of fluid into the quill. This check valve ensures that the chemical flows only in the desired direction.
  • Stabilizing Fin (Optional): In certain applications, the injection quill may have stabilizing fins or vanes attached to the body. These fins help stabilize the quill in high-velocity fluid streams, reducing vibration and potential damage.
  • Pressure and Temperature Sensors (Optional): In advanced quill assemblies, pressure and temperature sensors may be integrated to monitor the fluid conditions and provide feedback for process control.
  • Chemical Injection System: Though not a part of the quill assembly itself, the chemical injection system, such as a chemical injection pump or storage tank, is an essential component that feeds the chemical into the injection quill.

It’s essential to ensure that the materials used in the construction of the chemical injection quill assembly are compatible with the chemicals being injected and the fluids in the process to avoid any chemical reactions or material degradation that could affect the system’s performance and integrity. Regular inspection, maintenance, and monitoring of the quill assembly are also crucial to ensure safe and efficient operation.

Selection of Injection Quills

The selection of required injection quills depends on the following factors:

  • Retractable or Non-Retractable
  • Key dimensions like solution tube size, process connection size, insertion length, pressure class rating, etc.
  • Materials of Construction required.

Advantages of Chemical Injection Quills

The use of chemical injection quills offers several advantages:

  • Uniform Dispersion: The quill’s design ensures that the injected chemical is uniformly dispersed within the fluid stream, preventing localized concentrations and ensuring effective mixing.
  • Minimal Contact with Pipe Walls: The quill helps minimize direct contact between the chemical and the pipe walls, reducing the risk of chemical reactions or scale buildup that could hinder flow and affect system performance.
  • Precise and Controlled Dosing: Chemical injection quills allow for accurate and controlled dosing of chemicals, ensuring the correct amount is introduced into the system.
  • Easy Installation and Maintenance: Quills are relatively easy to install and maintain, making them a practical choice for various applications.

In conclusion, chemical injection quills are essential components in many industrial processes where precise and controlled chemical dosing is required. Their ability to uniformly disperse injected chemicals ensures effective performance and reliable results in diverse applications, ranging from water treatment to oil and gas production and beyond.

Types, Applications, and Selection of Choke Valves for Oil and Gas Operations

Choke valves or choker valves are a type of severe service control valve that is widely used in oil and gas production wells. They control the flow of well fluid. Additionally, Choke valves act to kill the reservoir pressure and regulate the downstream flowline pressures. A choke valve consists of a plug or stems that move up and down inside a slotted cylinder to control the flow.

Choke valves are very robust in design to handle severe extreme conditions of high corrosion, erosion, high fluid velocity, wide ranges of flow rates, marine environmental conditions, etc. It has the ability to handle extreme pressure drops in the range of 500 bars. Choke valves are usually designed based on API codes (API 6A/6D). Refer to Fig. 1 below that provides a typical cross-section of a choke valve.

Typical Choke valve Cross-Section
Fig. 1: Typical Choke valve Cross-Section

Applications of Choke Valves

Choke valves are found in a variety of applications. Some of the common uses of choke valves are:

  • Production well heads
  • For gas reinjection in the Christmas tree
  • In surface and sub-sea manifolds to handle mixtures of crude, gas, water, and sand in various chemical industries.
  • To handle Steam and CO2 in various petrochemical plants.
  • In drilling mud and hydraulic fracturing applications for oil and gas industries.
  • Oil and gas reserves.
  • Flowlines with very high operating pressure requirements.
  • Cementing and acidizing lines.
  • Oil and gas production platforms.
  • FPSO loading vessels.

Types of Choke Valves

Depending on the function of the choke valves they are classified into two groups. They are:

  • Regulating choke valves and
  • Non-regulating choke valves.

Regulating Choke Valves

This type of choke valve acts as a flow control valve. These valves are capable of maintaining steady production levels in production headers and flowlines. It is an automatic valve where an electric signal from the panel controls the opening of the valve.

Non-regulating Choke Valves

Non-regulating choke valves act as an On-Off valves. The opening of these types of choke valves is designed in such a way that it can remove pressure when in fully open condition. As the name suggests, they do not regulate or control the flow.

Depending on the orifice size, there are two types of choke valves.

  • Positive Choke valve having a fixed orifice size, and
  • Adjustable choke valves with a variable orifice size with an external adjustment device to vary the orifice size.

Depending on the design and construction of the choke valves they are grouped into the following types:

  • Needle and Seat Choke valve: simple design of positive choke with a cone-shaped plug, rising stem, and handwheel.
  • Plug and Cage choke valve: complex design with ported cages arranged to provide a great combination of flow and control capability.

The Port cage of the choked valve can be of various types like:

  • 4-port cage: Used for well-site separators and line heaters.
  • Multi-ported cage: for high-pressure drop critical applications.
  • Plug and cage design: for high-capacity applications.

Choke Design

To make better use of the gas for natural gas lift and to control the bottom hole pressure for recovery reasons, chokes hold back pressure on a flowing well. With decreasing hydrostatic head, the gas expands rapidly in vertical pipe flow, and the liquid moves in slugs through the tubing. This causes the potential gas lift energy to be rapidly lost. In turn, the liquids fall back and begin to accumulate over the perforations. These accumulating liquids hold back pressure on the formation. When enough liquids accumulate, the well may “die” and quit flowing.

The choke holds this backpressure by restricting the flow opening at the wellhead. The uncontrolled expansion and rise of the gas are restricted by the back pressure. It thus helps keep the gas dispersed in the liquids on the way up the tubing.

Chokes may have a variable or a set opening. The set openings, known as “beans,” are short flow tubes. They graduated in 1/64ths of an inch. Common flow sizes are about 8 through more than 20 (in 64ths) for small to moderate-rate gas wells.

Depending on the reservoir pressure, tubing size, amount of gas, and the amount and density of liquids, the size of the choke varies. To allow quick resetting, variable chokes may use an increasing width slot design. They are useful on well-cleanups following stimulation where choke size can vary over the course of a single day. They can also be used for periodic liquid unloading that necessitates frequent choke size changes.

Choke valve Symbols

Chokes valves are usually denoted by the following symbol in P&IDs.

Choke Valve Symbols
Fig. 2: Choke Valve Symbols

Functions of a Choke Valve

A choke valve mainly performs the following three main functions:

  • Changing the flow rate by controlling the choke cross-section.
  • Loading resistance, and
  • Pressure buffering by hindering the fluid flow to a certain extent.

Working Principle of a Choke Valve

The main purpose of a choke valve is to restrict the flow through the valve to have the desired flow rate. This is achieved by reducing the flow area through the valve body. The adjustable choke valves control the flow rate by adjusting the stem and seat combination. The handwheel can be turned to set the orifice size and flow coefficient which in turn produces the required flow rate. In the case of positive choke valves, a fixed flow rate is achieved through the use of a choke bean.

Selection of Choke Valves

Choke valves are carefully selected based on applications and various factors like size, material, trim design, etc. The parameters that influence the selection of choke valves are:

  • Inlet and outlet velocities
  • Cavitation index
  • Pressure drop limitation
  • Sound pressure level
  • Required flow rate
  • Process operating conditions
  • Start-up conditions
  • Size and Schedule of connecting pipework.
  • Physical properties of fluid handled

Advantages of Choke Valves

Choke valves are widely used in oil and gas production facilities because of their reliability and safe handling of high operating pressures. The main advantages of choke valves are:

  • High reliability
  • High rangeability
  • Controlled erosion
  • Low noise
  • The ability of pressure balancing
  • Accurate flow rate adjustment
  • Long service life

Further Studies

More details about the choke valves can be accessed by clicking here.

What is a Cold Box in Cryogenic Plants-Air Separation Unit

Cryogenic plants play a vital role in the production and processing of gases at extremely low temperatures, such as liquefied natural gas (LNG), liquid oxygen (LOX), and liquid nitrogen (LIN). At the heart of these facilities lies a crucial component known as the “cold box.”

What is a Cold Box?

A cold box is a specialized enclosure that houses key cryogenic equipment, such as heat exchangers, distillation columns, and other components necessary for the liquefaction and separation of gases. Its primary purpose is to maintain low temperatures while minimizing heat transfer from the external environment, ensuring optimal performance of the cryogenic processes.

Key Functions of a Cold Box

  • Thermal Insulation: The cold box is designed with advanced insulation materials to reduce heat ingress. This insulation is critical to maintaining the extremely low temperatures required for cryogenic operations.
  • Separation and Liquefaction: Inside the cold box, the gases undergo processes like distillation and heat exchange. The design facilitates the efficient separation of different components based on their boiling points.
  • Safety Containment: The cold box also provides a safe environment for operating cryogenic processes. It is equipped with safety features to handle pressure fluctuations and prevent leaks.
  • Condensation and Phase Change: The cold box allows for the condensation of gases into liquids, which is essential for transporting and storing cryogenic fluids.

What is a Cold Box in an Air Separation Unit?

The cold box in an air separation unit is a highly engineered large rectangular box enclosing the major cryogenic equipment. Some suppliers use a round silo design in which the equipment is primarily supported by the cold box foundation. The cold box wall is made up of steel panels that are welded onto the cold box frame. The space between the cold box wall and the equipment is filled with insulating material.

The cold box frame and foundation are designed to support the weight of all process equipment, as well as piping and valves containing the maximum operating level of liquid. It must also withstand high wind loadings as required by national codes and be suitable for the earthquake zone in which it is installed.

In air separation plants you can see square columns installed. Those are actually cryogenic cold boxes used to minimize heat leakage to the environment. The temperature inside the cold box is usually in the range of -196 Deg C. To prevent heat transfer vacuum is used.

Insulating Material used in Cold Box

The insulation material used in a cold box is either perlite, a fine powder, or slag wool, similar to glass wool but denser.

Typically, perlite is used for insulating the bulk of the cold box where access is unlikely to be required. Slag wool is used in areas where access may be necessary as it can be removed more easily than perlite. Slag wool is typically used in turbine, pump, and valve boxes.

Equipment housed in a Cold Box

The common equipment housed within the cold box typically includes:

The equipment associated with the cold box typically includes:

  • adsorbers
  • cryogenic pumps
  • expansion turbines.

Access to the internal equipment of a cold box is not possible during operation. Hence, all equipment functions are controlled through valves with extended stems that pass through the cold box wall. Access to the valves in a cold box for operation and maintenance is usually provided by a series of linked platforms and stairs or ladders.

Why does water cause a hazard to the Cold Box?

Water entering a cold box will freeze. It can become a hazard by preventing piping from free movement or causing excessive weight loads.

Ice may greatly extend the time required when a cold box is thawed. Therefore, it is extremely important to maintain the integrity of the seal at an opening (for example, at the valve and piping seal boots and manways). Water should be prevented from pooling on any horizontal surface.

Cold Box Purging

If the space inside the cold box contains air then oxygen could condense on liquid nitrogen pipework and create a hazard, also moisture can form ice in the perlite or slag wool, reducing the insulation and making it difficult to remove.

The insulation space inside the cold box is filled with nitrogen for this reason. This is known as the cold box purge. The cold box purge must be maintained whenever the cold box equipment is at cryogenic temperatures. It is usually maintained at other times also, except during internal work on the cold box equipment.

Different Types of Piping Involved in Cold Box

There are four types of piping involved in a cryogenic cold box:

1. Process piping

The process piping is used to carry fluids between the equipment items. Process pipes in a cold box vary in size from the very large low-pressure waste piping (up to 36 inches (0.9 m) on a large tonnage ASU) to small liquid lines such as liquid argon product (1 inch, 25 mm). Click here to know more about Cryogenic Piping.

2. Relief Valve Piping

The Relief valve piping connects pressure vessels to external pressure relief Valves. The major pressure relief pipes are for the high-pressure and low-pressure columns. These may have to handle large flows of gas with small pressure drops and can therefore be large in diameter. They must discharge to safe locations because of the potential for very high oxygen or nitrogen concentrations and low temperatures and are typically routed to the top of the cold box.

3. Vent, Drain, Purge Piping

Purge, vent, and drain piping which connects process equipment and process piping to the outside of the cold box for the supply of services, such as dry air or N2, and to allow venting of process gases or purge gases to the atmosphere.

These pipes are typically in the range of 4 to 1 inch (100 to 25 mm) in diameter. Purge and drain connections are usually found near the base of the cold box and maybe in groups connected to headers. Purge connections to process piping are made to the top of horizontal lines or to the side of vertical lines. For process pipes that can contain liquid, the thaw line must have a vertical lute of at least 1.5 ft (500 mm) to provide a vapor seal and prevent the backflow of liquid to the purge system.

Whenever possible, thawing and drain lines are run close to the cold box face to gain heat to maintain a warm gas seal to the valves. The liquid drain headers are connected to safe liquid disposal areas. The exhaust plume from vent piping may be O2 enriched or depleted. Vents must be located so that personnel cannot enter the plume until it has mixed with sufficient air to reach a concentration in the range of 19 to 25% O2.

Drains and vents may discharge liquid or very cold gas and must be positioned so that personnel is protected from contact and that discharge flows do not impact temperature-sensitive material and equipment.

4. Instrument piping

Instruments are connected from outside the cold box through the cold box face to the equipment items and the process piping by instrument piping. Instrument piping may also be known as impulse lines. The term instrument (for example, pressure, analysis, flow) tap also designates the connection from the valve at the cold box face to the internal process equipment.

Instrument piping is small-bore since flows are typically very small (to analyzers), or zero (for pressure, level, and flow instruments). The minimum size is determined by practical requirements for strength to withstand loads imposed by movement due to shrinkage or manual loads during cold box manufacture and maintenance.

Instrument connections are grouped at the cold box face into panels. This is for allowing easy access to both permanent and temporary instrument connections.

Why warm seal is provided in the cold box safety valve line?

To prevent relief valves from being permanently cold a warm gas seal is created on the piping. The piping runs vertically upwards from the box penetration by at least 750 mm (2.5 ft). Where feasible, the line within the cold box is routed close to the box face prior to the box penetration.

What material is used for piping?

Piping is usually manufactured from aluminum, although stainless steel and copper alloys are used in some services. All three materials remain ductile at cryogenic temperatures. Carbon steel is not used because it becomes brittle and may fail at temperatures below –29°C.

Why does a cold box require flexibility? How is the flexibility provided?

Equipment in a cold box shrinks when in operation. For example, the height of a 60-meter (197-ft) high distillation column may shrink by approximately 230 mm (9 in) when cooled to operating temperature. All the piping attached to the equipment must accommodate this shrinkage. Flexibility is provided by a series of turns in the piping, usually by a sequence of vertical and horizontal sections.

Supporting Cold Box Pipes

The long lengths of piping in a cold box require support at regular intervals. Various types of support are used which either provide a fixed anchor or allow controlled movement.

  • Horizontal runs of large pipes may have spring-assisted supports to allow controlled movement.
  • Vertical pipe supports may allow sliding movement.

What safeguard follows to minimize leaks inside the cold boxes

Once equipment and piping have been insulated, access for any repairs becomes extremely

expensive. To minimize piping leaks, all piping joints in the perlite region of a box are welded. Special transitions are required for any unavoidable transition joints between incompatible metals (for example, aluminum to stainless steel). Where it becomes absolutely necessary to use flanges connections, these are placed in a separate internal box which is insulated with slag wool. This allows access without having to remove the perlite from the larger cold box.

How does Cold Box Accommodate Shrinkage?

Shrinkage of vessels and piping in operation causes movement of piping and valves relative to the cold box surface. The amount of movement increases with box elevation. This movement is accommodated by a flexible rubber boot placed between the box face and the valve stem.

Valves in Cryogenic Service

Valves used in cryogenic service have the same functions and duties as in any other process service but have some additional requirements for operation at low temperatures. Special requirements related to materials of construction and installation.

The valve body is contained within the cold box, with the stem extending through the box wall. Both stem and bonnet are usually manufactured from type 304 or 316 stainless steel, which has the necessary strength coupled with low thermal conductivity. The bonnet is an integral part of the valve body, with the stem seal located at the warm end of the extension external to the cold box

The type of cryogenic valve used is determined by service needs such as range of control, and allowable leakage when closed but may also be limited by practical issues such as weight and availability.

  • Cryogenic globe valves are typically used to a diameter of 150 to 200 mm (6 to 8 inches).
  • Butterfly valves are used for larger services.

Design Considerations

The design of a cold box is complex and requires careful consideration of various factors:

  • Materials: The materials used in constructing a cold box must withstand low temperatures and high pressures. Common materials include stainless steel, aluminum, and specialized alloys.
  • Insulation Technology: Multi-layer insulation (MLI) or vacuum insulation techniques are often employed to achieve the required thermal efficiency. These methods minimize heat transfer and keep the internal environment stable.
  • Size and Layout: The dimensions and configuration of the cold box depend on the specific applications and the volume of gases being processed. Proper layout ensures efficient flow and minimizes dead spots where heat could accumulate.
  • Safety Features: Given the risks associated with cryogenic materials, cold boxes are equipped with safety relief valves, pressure monitoring systems, and emergency shutdown mechanisms.

Applications of Cold Boxes

Cold boxes are used in various industries, including:

  • Natural Gas Processing: In LNG plants, cold boxes are essential for liquefying natural gas, allowing for easier storage and transportation.
  • Medical and Pharmaceutical Industries: Cold boxes play a role in producing liquid oxygen and nitrogen for medical applications, ensuring the safe delivery of critical gases.
  • Aerospace and Defense: Cryogenic technologies are vital in aerospace for rocket propellants, making cold boxes crucial for testing and production.
  • Industrial Gas Production: Cold boxes are also used in the production of industrial gases, such as argon, krypton, and xenon, through air separation processes.

Benefits of Using a Cold Box

  • Enhanced Efficiency: By optimizing the conditions for gas liquefaction and separation, cold boxes significantly improve the efficiency of cryogenic plants.
  • Cost-Effectiveness: Reduced heat transfer and improved thermal management lead to lower energy consumption and operational costs.
  • Improved Safety: Advanced design and safety features in cold boxes minimize the risks associated with cryogenic operations, protecting both personnel and equipment.
  • Space Optimization: Cold boxes can be designed to maximize space usage, allowing for more compact plant layouts while still maintaining operational efficiency.

The cold box is a fundamental component of cryogenic plants, enabling the efficient processing of gases at extremely low temperatures. Its sophisticated design, combined with advanced insulation and safety features, ensures optimal performance while mitigating risks.

More details about cryogenic valves are already covered in the following article: What is a Cryogenic Valve? Features and Applications of Cryogenic Valves

An Overview of Linear and Non-Linear Analysis in Piping Stress Calculations

In reality, the behavior of any system is not completely linear. Linear analysis can only approximate the behavior of the system to an extent. Generally, Non-linear behavior may be due to,

  1. Geometry,
  2. Material and
  3. Boundary conditions.

In Piping stress analysis,

  • Geometry non-linearity is taken care of by means of Stress Intensification factors (SIF).
  • Material nonlinearity is not considered, as the material is considered to be in the elastic limit.
  • However, in Elasto-plastic analysis (For e.g. Blast), Material non-linearity shall be considered.
  • Boundary condition non-linearity means having non-linear restraints (+Y), Supports with Gap and Friction.

However in Linear analysis (Linear Boundary condition)- Rigid restraints (two-directional) are to be used, No support gaps to be used and the effect of friction to be neglected.

The Static stress problems are solved by first assembling the equation,

[K]{X} = {F}

Where,

  • K is the global stiffness matrix of the piping system,
  • X is the unknown Nodal displacement vector,
  • F is the known Nodal load vector (For each load case).

In Non-linear analysis, this Stiffness [K] changes during the iteration sequence when solving for
displacement in a particular load case. For e.g. When there is Rest support in a piping system, and if the pipe lifts off, then [K] is adjusted to remove the stiffness of that restraint. In Non-linear analysis, each Operating load Case (for particular support) could produce a different sustained stress distribution.

Whereas in Linear analysis, the model stiffness never changes since there are no Non-linear restraints,
those equations are assembled and solved just once for each load case, and stiffness is not updated
when the Piping system is deforming. Thus linear analysis follows a straight path. In stress analysis software packages the time taken by the software for convergence is lesser in linear analysis, whereas, in Non-linear analysis, the time taken is more because the stiffness is changed continuously.

Lift-up Support

If a Support lifts up in an operating cycle, it means it is inactive and the piping loads are distributed to
other supports in the vicinity, hence increasing the sustained stresses and with temperature, expansion
stresses change. When this operating cycle is maintained for a period, Sustained stresses remain the
same as there are no further lifts up of other supports in the system. Also, the expansion stresses will be
reduced due to yielding. During a shutdown, the pipe moves back to the support and hence the sustained stresses are reduced as the pipe comes (all supports become active) to its original cold condition.

If considerable yielding occurs in hot conditions, the pipe may return to the support point before the temperature reaches the ambient temperature. A continued cooling down to ambient temperature will cause very high thermal stresses and loads due to stoppage by the support which prevents the pipe from moving further down.

Generally, it’s good to avoid lift-up supports in a piping system as its inactive during operation. In linear analysis, we model Rigid supports. In some cases, lift-up supports may be required due to layout constraints.

In offshore projects, it is recommended to use support with Hold down in case of lift-up due to occasional load cases, if it’s not possible to avoid lift-up support. Hold-down supports with higher upward loads may cause overstress of the pipe. Providing Hold down still means the pipe is not seated on the structure in the operating case!

If the piping system has lift-up supports, it is mandatory to check all the stresses by removing the lift-up
support (Hot Sustain check). While calculating the Full displacement stress range, if liberal stress is activated, then we have to remove the lift-up support and calculate the full displacement stress range.

From ASME B31.3 302.3.5(d),

Allowable Displacement Stress Range, SA = f (1.25Sc+0.25Sh).

If we are activating Liberal Stress, it means we are using the difference between Sh and SL in the above
equation.

(Generally, SL will be lesser than Sh). Then, SA = f [1.25(Sc + Sh) – SL].

In the case of lift-up supports, this has to be taken care of. Removing the inactive supports during hot conditions may increase the sustained stress SL. Hence, the Liberal stress allowable would be lesser.

Here,

  • Sc = basic allowable stress at minimum metal temperature expected during the displacement cycle under analysis= 138 MPa (20 ksi) maximum.
  • Sh = basic allowable stress at maximum metal temperature expected during the displacement cycle under analysis= 138 MPa (20 ksi) maximum
  • SL = stress due to sustained loads; in systems where supports may be active in some conditions and inactive in others, the maximum value of sustained stress, considering all support conditions, shall be used.

From CAESAR II 2016 edition onwards, the Hot sustain stress is been incorporated in load cases for
each temperature case. It calculates the Full Displacement stress range stress with liberal allowable
activated by removing the lift-up support.

The below table gives the details about Load cases considered in Linear and Non-Linear calculations.
Here, operating conditions are considered in Non-linear calculations.

Table showing Linear and non-linear load cases in Caesar II
Fig. 1: Table showing Linear and non-linear load cases in Caesar II

If some of the boundary conditions are non-linear (For e.g. If some lift-up supports) all load cases should
be evaluated considering an operating case.

Sustained case- (W+P1+T1)-T1 = W+P1
Occasional case- (W+P1+T1+WIN1)-(W+P1+T1) = WIN1 etc.,

If all the boundary conditions are linear in a piping system, the Sustained case is not impacted with respect to operating conditions.

Let us consider an example of a Pump Discharge system as shown in Fig. 2 below

A typical Pump Discharge System
Fig. 2: A typical Pump Discharge System

The above piping system is solved using Linear analysis with some lift-up supports at Nodes 10700, 11300, 11900, and 12500 let’s compare the results of the Sustained case (with and without considering operating conditions) with the same system by changing lift-up (Non-linear) into Rigid Z (Linear).

Load cases and Output Results
Fig. 3: Load cases and Output Results

It can be inferred that with the lift-up supports, load changes are observed in the Sustained case with and without the operating case.

Support with Gaps

A restraint with a gap is also a form of nonlinearity. Hence operating effect is to be considered. Practically at the site condition, it’s not possible to maintain a zero mm gap in supports (The construction gap is a maximum of 2 mm.

Hence it may be without a gap or it may have a 2 mm gap. So, shall we use this advantage to solve the stresses and Nozzle loads in our Piping system? which may reduce additional flexibility (Elbows, more
compensation leg etc.,)

Pipe supports are used to take loads (Sustained, occasional, etc.) so that overloads induced by Piping
is not transferred to the equipment nozzle and to safeguard the Nozzle. So solving the equipment nozzle
using support with gaps near the nozzle may not guarantee that this support will take the load in all
operating scenarios.

For example,

Consider a line that has a design temperature of 120°C and an operating temperature of 50°C. In this case, the line will be mostly operating at 50°C and it may or may not fluctuate between 50°C to 120°C when the plant shutdowns, it will be at ambient condition. Hence, the support considered with the gap may not take loads at a certain operating condition which may result in overloading of the nozzle. Hence, it’s not good engineering practice to consider support with gaps near the nozzle to solve them.

It is good practice that the nozzle loads shall be checked without a gap and with a 2 mm gap up to a certain point. (i.e. maybe up to two rest, guide, stop varies on the situation). But whether support with gaps can be considered (as per the Stress engineer’s view) to solve high expansion stresses? if it’s not possible to change the routing, to give adequate flexibility, and reduce the additional piping components (Cost factor!) with a good engineering approach.

If we are using supports with gaps to have flexibility, then it is better to check loads, stresses and
displacements for both design and operating cases even if operating is far less than design.

Support Friction

As friction always opposes the motion, the effect of friction on a piping system can be advantageous in some scenarios, and may be non-conservative to ignore it in some scenarios. Please refer to the paper, “Treatment of Support friction in Pipe Stress Analysis” by LC Peng for a detailed explanation of Friction in the Piping system, which gives a detailed explanation of the behavior of support friction.