๐ฌ Live Stream: DREAM Refinery — India | Project Introduction and Configuration
๐ข Live Stream Announcement
๐ด LIVE SESSION: "A New Integrated Refining Complex for India – The ppPLUS Dream Project Configuration"
We’re excited to invite you to our very first Molecules to Market live session, where we unveil the Virtual Refinery “Dream Project” built on the ppPLUS platform!
JoinSanjay Gupta,Uwe Braun, andDr. Nicolas Kokelas they walk you through a fully integrated refining complex for India – configured, visualized, and analyzed live on ppPLUS, our open, collaborative platform for the process industries.
๐ Date: Saturday, September 5th
๐ Time:
17:30 hrs (India)
16h00 hrs (UAE)
15:00 hrs (KSA)
14:00 hrs (CEST)
13:00 hrs (UK)
08:00 hrs (EDT)
โฑ๏ธ Duration:
~1 hour (with extended Q&A)
๐ Streaming live on
What’s on the agenda
โ Introduction to ppPLUS – open access, collaborative, building a model of the global refining and chemical industry
โ The Dream Project on ppPLUS – entity & site pages, mass balances, and site configuration visualization
โ Live configuration deep-dive with the ppPLUS Configurator:
• Core refinery
• Olefins and aromatics integration
โ Interactive discussion – bring your questions!
This session is interactive – we’ll be answering your questions live throughout the stream, so come curious!
Whether you’re in refining, petrochemicals, technology licensing, engineering, or project development – this is your chance to see how a complex industrial site can be configured, analyzed, and shared collaboratively in the open.
๐ Save the date, set your reminder, and join us live!
๐ Like what you see? Register on ppPLUS and comment on the project yourself.
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ppPLUS has made a point from the design of its data-structure to model processes and operations,
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Ethylene Oxide is reacted with Water under neutral or acidic conditions, to form stepwise a range of products (Fig. 1)[1]:
When n = 1, the product is ethane-1,2-diol often known as monoethylene glycol HOCH2CH2OH, used in engine coolants, in heat transfer fluids, and for production of polyesters such as PET (polyethylene terephthalate).
When n = 2, the product is HOCH2CH2OCH2CH2OH, usually known as diethylene glycol. It is used principally to make polyurethanes and polyesters.
When n = 3, the product is HOCH2CH2OCH2CH2OCH2CH2OH, also known as triethylene glycol and which is is used as a plasticiser.
When n = 4 or more, the product is a poly(epoxyethane), known usually as polyethylene glycol (PEG). These are classified by relative molecular mass, PEG200, PEG400, PEG600, etc. and are used as nonionic surfactants, synthetic lubricants and solvents for paints. They are also used in cosmetics and are used as plasticisers in adhesives and printing inks.
Figure 1 - Production of ethylene glycols.
This reaction can be catalyzed by either acids or bases, or can occur at neutral pH under elevated temperatures. The highest yields of ethylene glycol occur at acidic or neutral pH with a large excess of water. Under these conditions, ethylene glycol yields of 90% can be achieved. The major byproducts are the Oligomers, and Tetraethylene Glycol[2].
Process Description
The process comprises two major sections (Fig. 2): (1) Ethylene glycol synthesis; and (2) Ethylene glycol purification[3].
Ethylene Glycol Synthesis
The ethylene oxide is combined with water, heated and fed to a tubular reactor, where the ethylene oxide is thermally hydrolyzed to Ethylene Glycol without a catalyst. As ethylene oxide reacts with ethylene glycols more quickly than with water, diethylene glycol (DEG), triethylene glycol (TEG) and heavy glycols are also formed. The yields of such glycols, however, are minimized by conducting the reaction in excess of water, what ultimately improves selectivity towards MEG[3].
Purification Section
The excess of water used in the EG reaction is removed from the reactor outlet by means of a multi-stage evaporator. Then, the MEG is purified in successive distillation steps, while residual water is recycled to the reactor as process condensate and DEG and TEG are recovered as by-products[3]. However, the separation of these oligomers and water is energy-intensive[2].
Figure 2 - Simplified PFD of Ethylene Glycols from Ethylene Oxide Direct Hydrolysis
Copyright Simplified PFD of Ethylene Glycols from Ethylene Oxide Direct Hydrolysis https://medium.com/intratec-products-blog/ethylene-glycol-production-from-ethylene-oxide-direct-hydrolysis-economic-analysis-93dcd586e113
Copyright Simplified PFD of Ethylene Glycols from Ethylene Oxide Direct Hydrolysis https://medium.com/intratec-products-blog/ethylene-glycol-production-from-ethylene-oxide-direct-hydrolysis-economic-analysis-93dcd586e113
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