critical issues when building a new refinery or upgrading...
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RBD
Critical Issues when Building a New Refinery or Upgrading an Existing One
Ken Carlson RBD Technologies Inc., USA.
• Capital costs • Operating costs • Crude oil versus operating costs • Processing: Dry Fractionation Degumming/Neutralization Drying Bleaching Hydrogenation Interesterification Deodorization Vacuum Systems Controls Glass Scale Refining Lab • Summary
RBD
TOPICS Critical Issues when Building a New Refinery or Upgrading an Existing One
1000 TPD Refinery $ 50,000,000
RBD
Civil 25%
Tank Farm 12.5 %
Utilities 12.5%
Process HW 23%
Installation 25%
Engineering 2%
100 TPD Refinery $ 10,000,000
Civil 25%
Tank Farm 12.5%
Utilities 12.5%
Process HW 17%
Installation 25%
Engineering 8%
INVESTMENT COSTS Bigger is Less
Critical Issues when Building a New Refinery or Upgrading an Existing One
Depreciation 26%
(10 years, 5%)
Utilities etc. 25%
Labor 5% (20 x $60K/year)
Processing Loss 44%
Processing Loss 25%
Labor 29% (20 x $60K/year)
Depreciation 31% (10 years, 5%)
Utilities etc. 15%
1000 TPD Refinery $ 75/MT
100 TPD Refinery $ 125/MT
RBD
OPERATING COSTS Bigger is Less
Critical Issues when Building a New Refinery or Upgrading an Existing One
1000 TPD Refinery Total: $1,275/MT
100 TPD Refinery Total: $1,325/MT
RBD
Crude oil: $1,200/MT 94%
Operation: $75/MT 6%
Crude oil: $1,200/MT 91%
Operation: $125/MT 9%
OIL VERSUS TOTAL COST Cost of oil is dominant
Critical Issues when Building a New Refinery or Upgrading an Existing One
PROCESSING Chemical or Physical?
Refining Modification
Bi-product
RBD
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
Chilled Water Tank
Refrig System
Alternating Crystallizers Continuous
Option ?
Cooling Water
Slurry Circulation Pump
Stearin Filter
Stearin Melt Tank
Core Blow Tank
Stearin
Olein
Filter “Squeeze” Pump
Crude oil
Hot Olein Wash Tank
Cold Olein Rinse Tank
Olein Tank Fill Work Filter
Heater
DRY FRACTIONATION Continuous ?
Alternatives: drum filter
or centrifuges
Critical Issues when Building a New Refinery or Upgrading an Existing One
To Drying/ Cooling
Wash water effluent
Wash water Receiver
Separator
Acid Lye
Gums/ Soap
Soapstock Receiver
Heater/ Cooler
Cavitation Mixer ?
Separator
Mixer
Wash Reactor
Cavitation Mixer ?
Enzyme ?
Size/Design of Degumming/ Neutralization
Reactor
Type of Heater
Acid conditioned oil to Bleaching
Degummed or neutralized oil to Bleaching or Washing ?
Water
Feed Oil
Type of pump
RBD
DEG/NEUTRALIZATION Design for degumming and neutralization
Water washing for QA
Critical Issues when Building a New Refinery or Upgrading an Existing One
Degummed or neutralized oil
RBD
DRYING/COOLING Use when sending oil to storage
Heater Cooler Hot well
Vacuum Dryer
Steam
Recycle to cooling tower
Vacuum system
Water from cooling tower
Mechanical Vacuum Pump ?
Critical Issues when Building a New Refinery or Upgrading an Existing One
BLEACHING Basic Design
Bleaching Reactor
Heater
Adsorbent Filters
Precoat/Heel Tank
Filtrate Receiver
HR
Spent Adsorbent
Safety Filters
Hot oil to Deodorizing
To vacuum
Adsorbent Hopper
Dosing System
Cooled oil to Storage
Filter Aid
Degummed or neutralized oil
RBD
Steam mixing ?
Pulse Tube Filters ?
Precoat or recycle ?
Slurry Tank ?
Carbon ?
Optical on-line technology for measuring chlorophyll
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
Bleaching Reactor
Trim Heater
Adsorbent Filters (3-cycle operation)
Precoat/Heel Tank
Filtrate Receiver
Spent ads.
To vacuum
Earth Hopper
Earth Feeder
Safety Filters
Silica Feeder
Silica Mix Tank
Silica Hopper
Slurry Tank
To vacuum
Dryer
Heater
Filter Aid
Hot oil to Deodorizing
Vent Vent Water
2nd (earth) Filtration
1st (silica) Filtration
Clean
A B C
Degummed or neutralized oil
BLEACHING Silica pre-treatment and earth re-use for
less earth & oil loss
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
Reactor
Catalyst Filter
Precoat Tank
Spent Catalyst
Safety Filter
To vacuum
Filter Aid
Bleached oil
HR
Hydrogen
N2
To Post Bleaching
Drop Tank
Feed Tank
Flash Tank
Catalyst
Vent
HYDROGENATION For hard fats only
otherwise blending and/or IE
Dual Reactors For high capacity
Pulse Tube Filter ?
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
Reactor
Adsorbent Filter
Precoat Tank
Spent Adsorbent
Safety Filter
To vacuum
Dosing System
Filter Aid
Sodium Methoxide
Dosing System
Silica Earth
Citric Acid Dosing System
Heater
N2
N2
Interesterified oil
Drop Tank
Blended bleached oils
Pulse Tube Filter ?
INTERESTERIFICATION Batch Chemical:
For frequently changing recipes
Toxic
Critical Issues when Building a New Refinery or Upgrading an Existing One
INTERESTERIFICATION Continuous Enzymatic:
Lower operating cost, higher quality, non toxic
Courtesy of DeSmet Ballestra
RBD
Blended RBD oils
Vacuum Dryer Buffer Tank
Heater Cooler
Enzyme Preparation
Tank
To vacuum
To vacuum
To vacuum
To vacuum
Enzyme
Product Tank
Cooler
Safety Filters
Interesterified oils
4 –
6 In
tere
ster
ifica
tion
Reac
tors
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
BFW Cooler Filters Heater
Polish Filters
Cooler
Distillate
HR Cooler
Anti-ox System
High Pressure Steam Generator
Scrubber
To Vacuum
RBD oil
To Vacuum
Pre-heated Boiler Feed Water ?
Nitrogen
Steam
Product Cooler
Boiler Feed Water
BFW Surge Tank
Double Thermo siphon
Loops ?
Bleached oil
DEODORIZATION Semi-Continuous and
heating/cooling under vacuum for multiple stock changes
Critical Issues when Building a New Refinery or Upgrading an Existing One
HR Filters Heater
Polish Filters
Spar
ge S
team
N
itrog
en
Cooler
Distillate
Product Cooler
Alternating HR units ?
Heat-bleaching Section
Post Deodorizer
Anti-ox System
Distillate Receiver
Deaerator
Stripping Section
Double Shell?
High Pressure Steam Generator
Back-up Heater
Final Heater
Scrubber
Cooler
To Vacuum
RBD oil
Bleached oil
RBD
Electric ?
DEODORIZATION Continuous PC and heating/cooling under
pressure for minimum energy consumption
Critical Issues when Building a New Refinery or Upgrading an Existing One
Cooler
High FFA Fraction
RBD
Toco/Sterol Fraction
To Vacuum
Lo Temp Section
High Temp Section
Cooler
Vapor from Deodorizer
DEODORIZATION Two-stage scrubber for
max distillate value
Critical Issues when Building a New Refinery or Upgrading an Existing One
Steam
Cooling Water
Vapor from Deodorization
Vapor from Deodorization
Greasy Cooling Water
“Greasy” System “Clean” System
Clean water to Cooling Tower
Greasy water to Cooling Tower Effluent
Greasy water Cooler
Caustic
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VACUUM SYSTEMS Greasy or clean?
Barometric or surface
condensers ?
Steam
Hot Well Water Chiller
Critical Issues when Building a New Refinery or Upgrading an Existing One
Cooling Water
Hot Well Effluent
Steam Ammonia to Chiller
Ammonia from Chiller
Start-up jet
Muffler
In use Melting Hot
ammonia
Vapor from Deodorization
Ejectors
Melted fat
Ice Condensers Surface
Condensers
RBD
VACUUM SYSTEMS Ice Condensation:
Optimum for large plants
Critical Issues when Building a New Refinery or Upgrading an Existing One
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CONTROLS From hardwire to fieldbus
Some common terms:
RTU Remote Terminal Unit (converts sensor to digital data) PLC Programmable Logic Controller SCADA Supervisory Control Automation Data Acquisition HMI Human Machine Interface (PC) LAN Local Area Network WLAN Wireless Local Area Network
Traditional control technology: Hard wired with 4 - 20 mA analog field instruments Trends: • Fieldbus that allows multiple units per wire set as well as two-way communication with digital HART type instruments with EDDL • Wireless instruments for remote locations • Handheld communicators for linking with SCADA system • Special apps for smart phones ?
Some common terms:
Fieldbus Digital two-way data transfer (6 – 8 devices/cable) Ethernet Standard communications protocol for building LANs HART Highway Addressable Remote Transducer (communication protocol for smart hosts and devices) EDDL Electronic Device Description Language (for accessing instrument manuals in SCADA system)
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
CONTROLS Typical components of complete refinery
Item Deg/Neu Bleach Deo Tanks Other Total I/O’s 33 113 89 190 50 475 FIC/LIC 7 6 6 - 3 22 TIC 3 4 7 - 4 18 FT/LT/TT 3 16 32 35 4 90 LS/PS/TS 4 18 8 24 10 64
Critical Issues when Building a New Refinery or Upgrading an Existing One
Ice Condenser
Deodorizer with heating mantle and temperature control Gum/soap separator – 900 G
100 ml centrifuge tubes with conical bottom
High Shear Mixers
Filtration Funnel
Distillate Receiver
Titration Device
Hot Plate with
Stirrer
Bleached Oil
Receiver
Scales
Digital Vacuum Gauge
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LABORATORY Glass Scale Refining for QA
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
SUMMARY Key Points
• Plant size: Think big and/or specialized • Product vs operating cost: Oil price over 90% of total operating cost • Physical or chemical refining: Design for chemical • Dry Fractionation: Continuous under development (DeSmet) • Deg/Neutralization: Design for neutralization for QA Consider enzymatic degumming for yield gain Consider water washing for QA Consider cavitation mixing for less reagents • Bleaching: Consider earth re-use (green oils) • Hydrogenation: For making hard fats only • Interesterification: Consider enzymatic • Deodorization: SC for multi stocks, continuous PC for bulk Two stage scrubber for higher distillate value • Vacuum Systems: Consider “clean” or ice condensing designs
• Controls: Consider fieldbus & HART instruments
Critical Issues when Building a New Refinery or Upgrading an Existing One
RBD
THANKS FOR YOUR ATTENTION !
Critical Issues when Building a New Refinery or Upgrading an Existing One