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Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California, Irvine

Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Page 1: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Petroleum Refinery Unit

Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz

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Chemical Engineering and Materials Science

University of California, Irvine

Page 2: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Outline

●Introduction & Objectives

●Process Overview○ Process Flow Diagram○Heat & Material Balance○ Pump Calculations○ Equipment Sizing

●Economic Analysis○ Equipment Pricing○ Plant Cost Estimation

●Other Considerations○Health, Environment, etc.

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Page 3: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Introduction & Objectives

• Separate crude oil into “cuts” based on boiling point range

• Can be done at atmospheric and vacuum pressure

• First step in overall refinery process

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Page 4: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Process Flow Diagram

Crude Distillation Process

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Crude: 165,000 bpsd

Product: 164,834 bpsd

Page 5: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Heat Integration

● Used in estimating number of heat exchanger shells

● Large approach temp is cheaper, less efficient

● Additional cooling provided by air (>130F) and water (<130F) cooling

Page 6: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Pump Calculations

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● Used for pump sizing and cost estimation

● Centrifugal pumps:○ Most commonly used○ low cost○ easy to maintain/operate○ many diff sizes

● Pump Horsepower:

PH= (Q x

h)/3960

Page 7: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Equipment SizingHeat Exchanger sizing:

Column & Vessel sizing: Sauder’s and Brown Correlation:

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Page 8: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Equipment Pricing Tools

Scaling Factor: Cost Index:

*Chemical Engineering Plant Cost Index

“Equipment Cost” Link from Plant Design and Economics for Chemical Engineers Text<<http://www.mhhe.com/engcs/chemical/peters/data/ce.html>>

Page 9: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Pre-Design Cost Estimate

Page 10: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Capital Estimation Tools

Fixed Capital Investment = Direct Cost + Indirect Cost

Direct cost = 75% of Fixed Capital Investment

Total Capital Investment = Fixed Capital Investment + Working Capital

Working Capital = 15% of Total Capital Investment

Page 11: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Economic Analysis of Process Design

Page 12: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Economic Effects of Assumptions and Uncertainties

● Heat exchangers and vessels are carbon steel

● Centrifugal pumps are cast steel

● Investment data calculated from equipment cost○ Omit data such as insurance and contingency costs○ Six-tenths rule to scaling equipment size

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Page 13: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Engineering Code of Ethics

The Fundamental Principles of the NSPE Code of Ethics states that:

1. Engineers shall hold paramount the safety, health, and welfare of the public.

2. Engineers shall avoid deceptive acts.

3. Engineers shall perform services only in their area of competence.

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Page 14: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Environmental Regulations

Gas Emissions

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Page 15: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Environmental Regulations

Wastewater

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Page 16: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Environmental RegulationsNoise Pollution

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Page 17: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

Site Safety● Implement a good training program

● Check equipment and maintain process units on a daily or weekly basis

● Encourage personnel to report problems

● Make sure supervisors and operators are adequately trained

● Make sure there is adequate communication

● Make sure all employees are using adequate Personal Protective Equipment (PPE)

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Page 18: Petroleum Refinery Unit Bill Liang, Eric Severini, Leonora Kuzmenko, Nick Kurtz 1 Chemical Engineering and Materials Science University of California,

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Thank you