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Questions and Answers
What is the purpose of the Saturate Reduction System in the process?
To reduce the paraffin content of the alpha olefin product.
What is the pressure and medium used to heat the liquid in the tube side of E-320?
60 psig steam.
How is the nickel catalyst concentration adjusted in the Catalyst Blend Drum?
It is reduced from 2% to 0.2% using C14 as a diluent.
What happens to the NAO product after its residence time in the Catalyzed Mixing Vessel?
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Where is the nickel catalyst sourced from before being used in the process?
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What is the role of the Static Mixer M-320 in the Saturate Reduction System?
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How does the cooling process work for the NAO product in E-321?
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What happens after the liquid from the Reactor Effluent Separators is heated in E-320?
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What is the purpose of using C14 as a diluent in the Catalyst Blend Drum D-321?
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Describe the process flow from D-310A/B to T-340.
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Study Notes
Saturate Reduction System
- Designed to decrease paraffin levels in alpha olefin products.
- Facilitates the following stages of processing to enhance product quality.
Reactor Effluent Separators
- Liquid from D-310A/B is directed to E-320 (Catalyzed Product Heater).
- Heats liquid using 60 psig steam on the shell side for efficient processing.
Catalyst Injection and Mixing
- 0.2% nickel catalyst is introduced before the liquid reaches M-320 (Static Mixer).
- A thorough mixture emerges in D-320 (Catalyzed Mixing Vessel) ensuring effective reaction.
Cooling and Washing Processes
- The NAO product undergoes cooling in E-321 (Catalyzed Product Cooler) with cooling water on the shell side.
- After cooling, the product is further processed in T-340 (Caustic Wash Tower).
Catalyst Supply and Preparation
- 2% nickel catalyst is sourced from outside suppliers, stored in 55-gallon drums.
- Loaded into D-321 (Catalyst Blend Drum) equipped with M-321 (Blend Drum Mixer) for mixing.
- The concentration in D-321 is lowered to 0.2% using C14 as a diluent for optimal effectiveness.
Saturate Reduction System
- Designed to decrease paraffin levels in alpha olefin products.
- Facilitates the following stages of processing to enhance product quality.
Reactor Effluent Separators
- Liquid from D-310A/B is directed to E-320 (Catalyzed Product Heater).
- Heats liquid using 60 psig steam on the shell side for efficient processing.
Catalyst Injection and Mixing
- 0.2% nickel catalyst is introduced before the liquid reaches M-320 (Static Mixer).
- A thorough mixture emerges in D-320 (Catalyzed Mixing Vessel) ensuring effective reaction.
Cooling and Washing Processes
- The NAO product undergoes cooling in E-321 (Catalyzed Product Cooler) with cooling water on the shell side.
- After cooling, the product is further processed in T-340 (Caustic Wash Tower).
Catalyst Supply and Preparation
- 2% nickel catalyst is sourced from outside suppliers, stored in 55-gallon drums.
- Loaded into D-321 (Catalyst Blend Drum) equipped with M-321 (Blend Drum Mixer) for mixing.
- The concentration in D-321 is lowered to 0.2% using C14 as a diluent for optimal effectiveness.
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Description
This quiz assesses your understanding of the Saturate Reduction System and its role in reducing paraffin content in alpha olefin production. It delves into the specifics of reactor effluent separation, product heating, and catalyst injection processes. Test your knowledge on the various components and their functions within the chemical engineering framework.
