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This paper covers and evaluates a retrofit work for desalting trains grids in Saudi Aramco Khurais facility to accommodate water cut increases due to field maturity. The main objective of this retrofit work is to accommodate the increase in water cut (emulsified and free water) while enhancing the de-salting process with minimum modification scope and cost effective approach. This Paper is intended to: Presents the retrofit basis and compare old and new grids design. Presents the results of this optimization study along graphical representations. Highlights how this initiative increased the desalting trains efficiency and redundancy. The basic concept of the retrofit work is to change the grids in electrostatic separation vessels from the conventional tapered configuration to straight configuration. The original configuration was tapered configuration that is intended to maximize separation and balance the load on all transformers however the limitations of this configuration is in case of one grid shorted all other transformers will be shorted. Despite the available transformers capacity, however as the water cut increases the chances of water carry-over increases as well as emulsions which results in multiple outages of de-salting trains. Straightening the grids will help avoiding total outages of the transformer, so in case of one grid shorted, other two grids will be running with a higher load which provides redundancy, reliability and guaranteeing the quality targets. This modifications were evaluated from safety, process, electrical and cost life cycle point of view and assessed post retrofitting for 1 year against there pre-defined success majors that includes: Outage hours of dehydrator and/ or de-salter (Target less than 5 hours per quarter). Demulsifer chemical consumptions (Target reduction by 10% or more annually) Quality specification (Target maintaining BS&W and Salts within crude specifications of 0.2% and 10 PTB respectively even in case of 1 or 2 transformers shorted. This modifications succeeded in achieving the predefined targets in addition to a cost saving equivalent to US$ 120,000 due to demulsifer injection reductions (i.e Regular and emergency dosage). Figure 1 shows the change in grids configurations before and after retrofit work
This paper covers and evaluates a retrofit work for desalting trains grids in Saudi Aramco Khurais facility to accommodate water cut increases due to field maturity. The main objective of this retrofit work is to accommodate the increase in water cut (emulsified and free water) while enhancing the de-salting process with minimum modification scope and cost effective approach. This Paper is intended to: Presents the retrofit basis and compare old and new grids design. Presents the results of this optimization study along graphical representations. Highlights how this initiative increased the desalting trains efficiency and redundancy. The basic concept of the retrofit work is to change the grids in electrostatic separation vessels from the conventional tapered configuration to straight configuration. The original configuration was tapered configuration that is intended to maximize separation and balance the load on all transformers however the limitations of this configuration is in case of one grid shorted all other transformers will be shorted. Despite the available transformers capacity, however as the water cut increases the chances of water carry-over increases as well as emulsions which results in multiple outages of de-salting trains. Straightening the grids will help avoiding total outages of the transformer, so in case of one grid shorted, other two grids will be running with a higher load which provides redundancy, reliability and guaranteeing the quality targets. This modifications were evaluated from safety, process, electrical and cost life cycle point of view and assessed post retrofitting for 1 year against there pre-defined success majors that includes: Outage hours of dehydrator and/ or de-salter (Target less than 5 hours per quarter). Demulsifer chemical consumptions (Target reduction by 10% or more annually) Quality specification (Target maintaining BS&W and Salts within crude specifications of 0.2% and 10 PTB respectively even in case of 1 or 2 transformers shorted. This modifications succeeded in achieving the predefined targets in addition to a cost saving equivalent to US$ 120,000 due to demulsifer injection reductions (i.e Regular and emergency dosage). Figure 1 shows the change in grids configurations before and after retrofit work
This paper covers an optimization study at Aramco's Khurais processing facility to maximize NGL yield and minimize H2S content through HYSYS simulation. Model validation and identifying the confidence level of the model (prior optimization) approach and results are covered along with the realized results of the optimized operating envelope in simulation compared to field trial results. The optimization approach focused on flashing more light ends due to a pressure drop in both the condensate feed drum and condensate stripper column while reducing NGL heating to maximize C3+ yield while maintain H2S below 30 PPMv. The identified optimized operating enveloped was implemented and benefits were realized. The main conclusions and realized benefits of adjusting the operating parameters to the optimized operating envelope includes maximizing NGL recovery in the facility by more than 900 BPD while maintaining quality parameters within limits, reduced the steam consumption by more than 150,000 lb/day and creating more tolerance to process upsets and normal fluctuations. The novelty of this paper is that it describes a process to define the confidence level of the model prior to commencing the optimization on a pre-existing model. In addition, it highlighted a simple approach to maximize C3+ recovery while minimizing H2S content and energy consumption, which creates room for optimization opportunities in any gas plant with no gas sweeting system.
This paper covers an optimization study in Saudi Aramco Khurais Facility through data analytics and modeling to enhance NGL Quality and maximize C3+ Yield through Process Modeling and big data statistical modeling of correlations. The paper objective is to: Share the optimization approach and how it can be replicated. Presents the results and outcomes of this optimizations along with utilized big data approaches. The main concept of this study is to utilize a big data approach to analyze +5 million data point to discover unknown relations between various parameters that cannot be explained from process point of view. Moreover, the discovered relations and other parameters were further investigated through statistical models of correlations. The generated results were evaluated from process point of view to be utilized in enhancing NGL quality and maximize the yield through developing new process schemes and system modifications via HYSYS simulations followed by a field trials prior actual deployment on plant level. This optimization approach resulted in discovering three new process schemes to enhance NGL quality and maximizing product yield including: External vapor propane injection to stripper column to artificially increase the traffic in the column and maximize the yield where a portion of the propane will be condensed in the column and generate more liquid volume of the higher product value (i.e liquid NGL) Vaporizing a slip strip from generated NGL to increase the traffic in the column artificially to increase the confidence level in maintaining the product quality to 99.7% (i.e 3 standard deviation). Vaporizing a slip stream of OFF-SPEC product to artificially increase the traffic in the column and maximize the yield. The main outputs of this optimization are: Developing 3 novel process schemes for hydrocarbon condensate processing. Increasing the confidence level of maintaining product quality to 99.7%. Generating additional value of additional NGLrecovery. The novelty in this paper is the approach to utilize big data and multivariate analysis along with process modelling to identify hidden relations and factors impacting yield and product quality that resulted in developing new process schemes to increase NGL yield and the confidence in achieving quality specifications to 99.7%. This process along with developed process schemes can be replicated and add benefits to any gas plant that utilize stripper columns for NGL sweeting process resulting in multiple circular economy initiatives and ideas such as reducing reprocessing time, reducing feed stock and reuse of off spec products in better applications.
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