Crude Distillation (Topping) Unit - 25,000 BPD
Other Views - click image for larger view
Crude Distillation (Topping) Unit - 25,000 BPD Crude Distillation (Topping) Unit - 25,000 BPD Crude Distillation (Topping) Unit - 25,000 BPD

Crude Distillation (Topping) Unit - 25,000 BPD

Stock # 445
Capacity 25,000 BPD
Products Light and heavy naphtha, Kerosene, Diesel, Residual fuel, Atmospheric gas oil

Overview

Used 25,000 BPD Crude Refining Unit (Topping Unit) built in 1940. The unit was designed to process two types of crude oil feed: light crude of 34° API and heavy crude of 20° API. The unit is designed to be able to reprocess 1,500 BPD of out-side off-spec naphtha in addition to and concurrent with the 25,000 BPD crude fractionation. Provisions are included to handle off-spec conditions either (1) for too high a vapor pressure or (2) with too high an end point. Alternate feed locations are to the Main Fractionator for conditions (1) or to the Naphtha Stabilizer for condition (2). Process Temperatures: Crude Charge 100 °F, Naphtha Product (max) 100 °F, Kerosene Product (max). 125 °F, Diesel Product (max) 150 °F, Atmos. Gas Oil (max) 175 °F, Residual Fuel Oil 200 - 300 °F. Column size basis 87% of flood (max). The Naphtha Stabilizer is designed to stabilize the light naphtha product (Pre-flash Tower Overhead) to 9# RVP (max). Design includes capability for re-running up to 1,500 BPD of off-spec.

Major Equipment

Pre-flash Tower
Caustic Treaters
Crude Fractionator
Product Stripper
Kerosene Stripper
Diesel Stripper
Gas Oil Stripper
Pre-flash Overhead Accumulator
Fractionator Overhead Accumulator
Naphtha Stabilizer
Stabilizer Overhead Accumulator
Residue / Crude Heat Exchangers
Fractionator Overhead/Crude Exchanger
Fractionator Overhead Condenser
Diesel Coolers
Gas Oil / Crude Oil Heat Exchangers
Naphtha Product Cooler
Kerosene Cooler
Share
Download Plant Brochure |
SPECIFICATIONS RESOURCES
Year Built
1940
Year Shut
1982
Capacity
25,000 BPD

For additional information, visit the Resource Center

Similar Plants