create a process flow diagram separate streams of ethanol and TG’s are co-fed (with entrained ash) to a mixer. The mixer combines these materials into a single liquid phase, which is then fed into the reactor. The reactor operates at steady state. The FAEE product, along with glycerol co-product and unreacted ethanol and TG’s. A separator (distillation column) fractionates the reactor effluent into a stream of pure glycerol, a stream of pure FAEE, and a stream containingall of the unreacted ethanol and TG’s. The unreacted materials are sent to a splitter; a portion issent back to the mixer and recycled to the reactor, while the balance is purged (waste).
create a process flow diagram separate streams of ethanol and TG’s are co-fed (with entrained ash) to a mixer. The mixer combines these materials into a single liquid phase, which is then fed into the reactor. The reactor operates at steady state. The FAEE product, along with glycerol co-product and unreacted ethanol and TG’s. A separator (distillation column) fractionates the reactor effluent into a stream of pure glycerol, a stream of pure FAEE, and a stream containingall of the unreacted ethanol and TG’s. The unreacted materials are sent to a splitter; a portion issent back to the mixer and recycled to the reactor, while the balance is purged (waste).
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create a process flow diagram
separate streams of ethanol and TG’s are co-fed (with entrained ash) to a mixer. The mixer combines these materials into a single liquid phase, which is then fed into the reactor. The reactor operates at steady state. The FAEE product, along with glycerol co-product and unreacted ethanol and TG’s. A separator (distillation column) fractionates the reactor effluent into a stream of pure glycerol, a stream of pure FAEE, and a stream containing
all of the unreacted ethanol and TG’s. The unreacted materials are sent to a splitter; a portion is
sent back to the mixer and recycled to the reactor, while the balance is purged (waste).
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