Jackson Systems - Understanding Basic DDC Controls for Commercial Systems

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Ashley

DDC Controls Basics ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]

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This manual will be useful to both specifiers and implementers providing a theoretical grounding for preparing a control system functional specification for implementation on Industrial control systems consisting of PLC (Programmable Logic Controllers), HMI (Human Machine Interfaces / SCADA devices) or DCS (Distributed Control Systems). FOR MORE INFORMATION: http://www.idc-online.com/content/design-industrial-automation-functional-specifications-plcs-dcss-and-scada-systems-15

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The steam-to-dry gas ratio (SDGR) is an important parameter in high-temperature shift (HTS) reactions, particularly the water-gas shift reaction. It represents the ratio of steam (H2O) to the dry gas components, primarily carbon monoxide (CO) and hydrogen gas (H2), in the feed gas. The SDGR is typically expressed as the mole ratio of steam to the sum of CO and H2. The selection of an appropriate SDGR depends on various factors, including the desired conversion, product selectivity, catalyst characteristics, and process conditions. Here are some considerations regarding the steam-to-dry gas ratio: 1. Water-Gas Shift Reaction: The water-gas shift reaction involves the reaction of CO and steam to produce CO2 and H2. The presence of steam is crucial for driving this reaction and increasing the formation of hydrogen. Therefore, an optimal SDGR is necessary to promote the water-gas shift reaction and achieve the desired CO2 and H2 production. 2. Optimal Range: The optimal steam-to-dry gas ratio can vary depending on the specific catalyst and operating conditions. In general, an SDGR in the range of 1 to 3 is often used in HTS processes. However, the exact ratio may vary depending on factors such as temperature, pressure, catalyst composition, and desired product distribution. 3. Effect on Equilibrium: Increasing the SDGR tends to shift the reaction equilibrium towards the formation of CO2 and H2, as the excess steam drives the reaction forward. Higher SDGRs can enhance CO conversion and increase hydrogen production. However, excessively high SDGRs can lead to excessive water production, which may have limitations depending on downstream processing requirements. 4. Catalyst Sensitivity: The choice of catalyst can also influence the optimal SDGR. Some catalysts may exhibit higher sensitivity to the SDGR, while others may be less sensitive. Catalysts with better water-gas shift activity and selectivity may be able to achieve higher conversions and better control of product selectivity across a wider range of SDGRs. 5. System Constraints: The SDGR should be considered in the context of system constraints and downstream processing. Excessive water production can pose challenges in downstream separation and purification processes. Therefore, the SDGR should be balanced to ensure efficient process operation without compromising downstream operations. Optimizing the steam-to-dry gas ratio requires careful consideration of the specific process conditions, catalyst characteristics, and desired product distribution. It is often determined through a combination of experimental evaluation, kinetic modeling, and process optimization to achieve the desired conversion and product selectivity in HTS reactions.

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This presentation by Westermo’s Technical Lead Engineers Dakota Diehl and Benjamin Campbell, is an integral part of the Westermo webinar held on April 30th 2020, covering how to simplify your network management using Westermo software tools WeConnect and WeConfig. Watch the webinar session here: https://www.westermo.com/news-and-events/webinars/simplify-your-network-management-using-software-tools

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Koch Modular Process Systems, LLC (Koch Modular) provides process control system and automation solutions for standalone turnkey applications or integration within a customer's existing PLC, DCS, or SCADA infrastructure. Koch Modular engineers work directly with the customer to design a custom solution specific to meet their plant, industry, standards, and needs. Koch Modular can also assist in modification of existing control systems to upgrade or integrate enhanced functionality.

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SUN went through a significant IT improvement program in their Product Innovation processes, now covering the the complete product value chain with a complete, open and integrated solution. David was project leader for the SUN PLM transition project. In late 2009, Oracle acquired Sun Microsystems for $7.4B. As part of a large systems integration project, 2 instances of MatrixOne PDM were replaced with Agile PLM 9.3. The implementation began in January 2010 with Phase 1 going live on September 27, 2010. The first phase included core Agile PLM plus interfaces to mCAD and eCAD on the front end, and a downstream integration to Oracle's existing eBusiness Suite R12.1.3 via the Agile Design-to-Release Process Integration Pack (D2R PIP). The project comprised 4 phases of which 3 are now live, realizing true "art-to-part" enterprise PLM. David's presentation will cover the business issues encountered at the beginning of the implementation, the implementation methodology, the IT Topology and lessons learned. Prior to Oracle, David managed PLM projects for Apple, Brocade, Kodak, SanDisk, Kyocera, HP and others. Before that he managed mechanical design teams at Ballard Power, Kodak and others, and ran his own consulting business. As an Engineer he started out designing mechanical parts and assemblies using 3D solid modeling CAD systems and manual drafting.

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Jackson Systems is a leading direct-to-contractor HVAC controls manufacturer and distributor. We produce innovative products for the commercial and residential markets. Ease of installation is built into every design, providing the most contractor-friendly products in the industry. Strong technical support and free same-day shipping are the cornerstone of our excellent client service. Jackson Systems is “Controls Done Right.”

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