Advanced Process Modelling examples

Better, faster, safer decisions in all areas of the process industries

gPROMS®'s high-fidelity predictive modelling capabilities are applied to a wide range of design and operational challenges in many different industry sectors.

Typical examples of Advanced Process Modelling used for model-based innovation and model-based engineering – some performed by the customer, some by PSE Consulting – are listed below.

In virtually all cases, they have resulted directly in significant savings or enhanced revenue, or accelerated innovation and development. In many cases they have resulted in new understanding of the fundamental phenomena, allowing for informed decision making that results in better design and better operation.

Process design

  • Whole-plant optimisation of a new propylene oxide process
    Simultaneous optimisation of reactor and separation sections to achieve tens of millions of Euros' improvement in process economics. See Hydrocarbon Processing article €€€ savings. [Repsol]
  • Design of falling-film sulphonation reactor
    Determined optimal reactor design, operating conditions and start-up procedure to minimise off-colour product and reduce cleaning frequency. $$ savings. [US consumer goods manufacturer]
  • Design of new multitubular reactor for petrochemical process
    New design for reactor shell and optimal utilisation of catalyst. First design to achieve uniform yield from all tubes in multitubular arrangement; performed own detailed design and saved significant costs on reactor. [LG Chem, Ltd]
  • Design of optimal multitubular reactor for terephthaldehyde production
    See Hydrocarbon Processing article. [LG Chem, Ltd]
  • Design of new membrane separations
    Developed an easy-to-use tool for the client's engineers to be able to rapidly assess new gas separation designs, with the resulting gPROMS model incorporated in Hysys. [US industrial gases process licensor]
  • Design of new continuous and batch processes for production of norbornene and tetracyclododecene. Designed plant that can reliably process wide range of feedstocks, varying in proportion of the two main products (from 1:5 to 5:1); $$ revenue enhancement. [Japanese petrochemicals producer]
  • Optimal design of licensed large-scale industrial crystallization process
    Developed high-accuracy models to enable process licensor to optimise the design of a licensed large-scale industrial crystallization process, for enhanced process economics. [BP Chemicals]
  • Distillation of ethanol/water mixtures with the use of entrainers
    Optimised process and selected best entrainer for required task. [US petrochemicals producer]
  • Design of Heat Integrated Distillation Columns (HIDiC)
    Designed new distillation column which can run without reboiler, demonstrating 60% overall energy savings. [Japanese petrochemicals producer]
  • Design and operation of new pharmaceutical reactor
    Guided experimental programme for the identification of complex chemistry, then used resulting data for design of new reactor with improved mixing and mass transfer. Derived new batch operating procedure to minimise side reactions and impurities. [UK/Italian pharmaceutical manufacturer]
  • Design of novel multitubular reactor for Fischer-Tropsch production of designer diesel. Detailed AML:FBCR kinetic model linked to a CFD model of the shell side fluid dynamics proved the design without the need to build a pilot plant, saving $250K. [US technology company]

Equipment design

  • Design of novel multitubular reactor for maleic anhydride
    New reactor design with improved yield and selectivity currently under patent application. [US petrochemicals producer]
  • Desulphurisation of flue gases
    Designed new desulphurisation equipment an optimised operating conditions to ensure maximum removal of sulphur in order to comply with anti-pollution laws. [Chilean plant equipment manufacturer]
  • Design of liquefied natural gas (LNG) storage tanks
    Provided detailed loading/unloading dynamic models of LNG storage tanks to achieve $$ savings on compression equipment and energy use. [UK oil & gas supplier]
  • Design of new depressurisation vessel for African offshore oilfield
    Demonstrated that the use of expensive alloy was necessary for only small part of the vessel, saving $1.5m in construction costs. [BP]
  • Crystallization in in-line mixing equipment
    Studied particle size distribution formed in complex, non-standard crystallization device, aimed at achieving enhanced product quality and consistency. [US consumer goods manufacturer]
  • Development of optimal fibre production, involving detailed design of bushing equipment. [US glass fibre manufacturer]

Process development

  • Development of new process for methyl ethyl ketone (MEK)
    Analysed data from lab scale equipment to identify true reaction kinetics, which were then used in the design of full-scale process including novel gas/solid contacting device. Company now has own process [Japanese petrochemicals producer]
  • Development of low-cost process alternative for bis-phenol A production
    Developed design based on low-cost multitubular falling-film evaporator to replace large, expensive and difficult-to-operate scraped-surface vessel in a licensedchemical process resulting in $$$ saving and simplified maintenance. [Japanese chemical company]
  • Development of reforming microreactor
    Used high-accuracy model of microreactor using microkinetic and diffusion modelling to drive model-targeted experimentation to determine detailed reforming kinetics. Development accelerated significantly. [BP Chemicals]
  • Design and development of hydrogenation reactor
    Applied MBI techniques in design of reactor for unsteady state operations with potentially central role in Japanese hydrogen economy. [Japanese chemical company]
  • Development of new types of storage tanks for liquefied natural gas (LNG). Guided the experimental programme to assess the viability of these new designs, thereby reducing the number and cost of experiments by an order of magnitude. [UK oil & gas supplier]

Process operations

  • Optimisation of dioctyl phthalate (DOP) processes
    Optimised recipe for existing plant, resulting in doubling of profit margin. Designed new batch plants (including new operating recipe) for construction in various Asian countries, as well as designs for continuous plant to replace batch plant. [Japanese petrochemicals producer]
  • Optimisation of catalyst change-over frequency
    Determined optimal frequency for multiple-reactor styrene monomer production unit, resulting in new set of optimised operating procedures [Shell Chemicals]
  • Optimisation of methanol plant catalyst lifetime
    Optimised methanol plant operating conditions for maximum catalyst life, with simultaneous optimisation of catalyst formulation. See Hydrocarbon Processing article[Süd-Chemie]
  • Reduced batch time for batch crystallizer
    Optimised recipe for batch crystallization for pharmaceutical-grade lactose, identifying 44% reduction in batch time for same quality product. [Friesland Campina]
  • Optimal operation of crystallizer
    Derived optimal recipe for batch crystallizer, leading to much narrower particle size distribution and hence significant improvements in downstream solids handling leading allowing an increase in production. [UK pharmaceutical manufacturer]
  • Safety analysis of distillation column startup
    Performed highly detailed analysis of events involved in major industrial accident, resulting in identification key factors leading to the accident. [US refinery operator]
  • Start-up of air separation units
    Optimised start-up procedure for 3-column air separation plant, with model subsequently used in operator training system. [Japanese industrial gases supplier]
  • Batch polymerisation 35% improvement in batch time
    Achieved 35% improvement in batch time for complex batch polymerisation process. [UK polymer additives manufacturer]
  • Optimisation of expandable polystyrene (EPS) production
    Optimised batch recipe identifying 30% reduction in processing time with no change in product quality. [BASF]
  • Removal of CO2 from hydrocarbon streams using reactive absorption
    Optimised column operation, including utilisation of caustic soda and pumparounds, with accurate prediction of product composition down to ppb levels using advanced rate-based separation models. [Linde Engineering]
  • Multistream heat exchanger modelling
    Developed general model of multistream heat exchanger for use in operator training; development time reduced from envisaged 6 months to 15 days. [Honeywell Process Solutions]
  • Optimisation of heap leaching operations
    Provided detailed modelling of leaching operations for use in operational improvements. $$ energy savings [Chilean minerals company]
  • Optimisation of grade transitions in polyethylene
    Derived optimal policies from switching from one grade of polymer to another, while reducing the off-specification product by more than 60%. Savings in time equivalent to 1 week's extra production per year. [Norwegian petrochemicals producer]
  • Crystallization of bisphenol-A
    Troubleshooting and startup optimisation of large-scale multi-unit industrial crystallization process to obtain required crystal size distribution, resulting in benefits of millions of dollars annually in additional on-spec product, enhanced throughput and reduced energy cost. [Japanese petrochemicals producer]
  • Removal of volatiles from polymer particles
    Optimised operating conditions to ensure maximum removal of volatiles in column. [US petrochemical producer]
  • Development of optimal control scheme for azeotropic distillation unit
    Developed scheme that resolved long-term problems in controllability encountered over years of operation. [Shell Chemicals]
  • Development of economically optimal design for azeotropic distillation unit
    Redesigned the same unit, identifying around half a million dollars per annum saving. [Shell Chemicals]

Product design and development

  • Design of cardboard boxes for detergent powders
    Used detailed diffusion models to study permeation of moisture from air into boxes, and recommended changes in box design and thickness. [US consumer goods manufacturer]
  • Design of SOFC fuel cells
    Detailed design of the fuel cell, the fuel cell stack and the fuel preparation sub-system. [UK fuel cells developer]
  • Design of PEM fuel cells
    Detailed design of the fuel cell and the fuel cell stack. [Many US & Japanese fuel cells developers]
  • Provision of decision support for many aspects of fuel cell component and system design [Toyota, Samsung , Mitsubishi Heavy Industries, Ceres Power, others]

There are many, many more applications in many application areas where PSE or our customers have applied Model-Based Innovation or Model-Based Engineering techniques to great benefit. Please contact us for more details.

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