Philosophy and Strategy of Idemitsu for the Future of Petroleum

The 32nd JCCP
International Symposium
January 30,2014
Philosophy and Strategy of Idemitsu
for the Future of Petroleum Refining Industry
- In Pursuit of Harmony between Value of Hydrocarbons
and Conservation of Environment
Presented by
Itaru Matsuhiro 松広 格
Executive Officer & General Manager
Technology & Engineering Center
Business Activities of Idemitsu
Idemitsu Group
Core
Business
Qatar
UAE
Vietnam
Functional
Materials
Business
Laffan Condensate Refineries
Technical Research Centre
Nghi Son Refinery
Resource
Business
Expanding business
to the global market
Operating four refineries and two petrochemical plants
for Core Business in Japan.
1
Management Philosophy and Technology Strategy
Idemitsu Kosan was Established in 1911
by Mr. Sazo Idemtisu, the founder.
Practicing the founder’s concept of
‘Respect for Human Being’ in the conduct of
business through the history of Idemitsu
for over 100 years.
Environmental Preservation
by Management Philosophy and Technical Innovation
Vision of the Petroleum Refining Industry Farther into the Future.
2
Environmental Preservation as Management Philosophy
‘Customers First’ : Consider customer satisfaction and act accordingly
1967 Constructed World First Resid HDS
1983 Launched Unleaded High Octane
Gasoline First in Japan
1993 Launched Low Benzene Gasoline
First in Japan
2005 Launched Sulfur Free Gasoline &
Diesel Fuel
3
Environmental Preservation as Management Philosophy
Harmony with Communities: Contribute to the development of local community
as a good corporate citizen.
1957 Construction of
Tokuyama Refinery
The refineries incorporated a green belt
intended to harmonize
with the natural surroundings.
1963 Construction of
Chiba Refinery
1973 Construction of
Hokkaido Refinery
1975 Construction of
Aichi Refinery
Certified by
Social and Environmental Green Evaluation System
4
Balance between Value of Products and
Preservation of Environment
Petroleum
Products
Petrochemical
Products
Catalysts
By Products
Process Energy
Minimize
Environmental Impacts
Waste Material
Waste Heat
Refinery
Maximize
Value of Products
Crude Oil
Naphtha
To Balance the Trade-Offs by Technology:
Future Vision of Refining Industry
5
Value Chain of Idemitsu: High Performance Plastics
Polycarbonate
Syndiotactic PS
Low Modulus PP
6
ARDS-RFCC Upgrading
Environ. Impact
:Maintain
Atmospheric
Residue
Atmospheric
Residue
VAC
Vacuum
Residue
OCR/RDS
Product Value
Add:Maximize
Maximize
RFCC
Gasoline
Diesel Fuel
Purpose: Maximize Charge of Vacuum Residue to RFCC
Condition: Control Catalyst Deactivation (Maintain Value of Products)
Approach: Predict and Use up the Activity in the Run Length
Steps of Approach
Analyze Influence of Asphaltene
and feed type to catalyst life
Optimize combination of feed
type and throughput
Catalyst
Activity
Index Influence of feed type and
throughput to the catalyst life
Unused
×
Minimum
Activity
×
OK
Shortfall
time
Plan to maximize throughput
of heavy bottom within the life
Reduce feed cost &
use up of the catalyst life
7
Ⅰ Catalyst Regeneration(RDS)
Product Value
Add:Maintain
Environ. Impact
:Minimize
Purpose : Reduction of catalyst waste and catalyst cost
by regeneration of used catalyst
Condition: Recover 1 year of catalyst life
(comparable performance as fresh catalyst)
Approach: Determine optimum regeneration conditions
Regeneration Ratio
Of Spent Catalyst(RDS)
25%
Mild
Regeneration
condition
Severe
6%
Japan
Idemitsu
Reference: hydroprocessing(2000) p.407
8
Ⅱ By-Product Recycle
to FCC
Environ. Impact
:Minimize
Product Value
Add:Maintain
FCC
By-Products
Petrochemical Plant Residue in middle
distillate range
Low polymers (PE, PP)
9
Ⅲ Energy Conservation
Environ. Impact
:Minimize
Product Value
Add:Maintain
Improved energy efficiency
more than 15% in the past 20 Years
Energy Conservation by TPM
TPM:
Total Productive Management
Energy Conservation Task Force
(company-wide activity)
Energy
Efficiency
(%)
target
▲15%
Fiscal Year
10
Optimization of Cleaning Cycle of Heat Exchangers
Purpose:
Optimize Cleaning Cycle of Heat Exchangers
Conditions: Balance Cleaning Cost and Energy Conservation
Approach:
Estimate Quantitatively Fouling of Heat Exchangers
Saved 9,000 (kl/y) of energy
U値
Fouling Index
500
400
Estimate Heat Exchanger Fouling Index
of the end of 2 years’ operation in
the first few months.
⇒ Determine Optimum Cleaning Cycle
300
200
100
0
Opening and Cleaning
Day
11
Ⅲ Energy Conservation
Environ. Impact
:Minimize
Product Value
Add:Maintain
Improved energy efficiency
more than 15% in the past 20 Years
Energy Conservation by TPM
TPM:
Total Productive Management
Energy Conservation Task Force
(company-wide activity)
Energy
Efficiency
(%)
Advanced
Process Control
Real Time
Optimization System
target
▲15%
Fiscal Year
12
Optimization of Utilities (Total Utility Management)
Operation Scheduling:
Utility Scheduling:
Purchase
Crude Oil Processing and Process Operation
Schedule based on Market Demand
Need detailed coordination of operation schedule
and utility supply balance.
Develop Cost minimum utility
supply plan in real time
Hydrogen
Purchase
Crude Oil
Refinery
Fuel
Refinery Processes
Weekly Operation Schedule
Steam
Products
Electric
Power
Purchase
& Selling
13
Ⅲ Energy Conservation
Environ. Impact
:Minimize
Product Value
Add:Maintain
Improved energy efficiency
more than 15% in the past 20 Years
Energy Conservation by TPM
TPM:
Total Productive Management
Energy Conservation Task Force
(company-wide activity)
Energy
Efficiency
(%)
Advanced
Process Control
Real Time
Optimization System
Operation
Management
System (XHQTM)
target
▲15%
Fiscal Year
14
Optimization of Utility Supply (Management by XHQTM)
Enabling refinery operation information sharing simultaneously and in real time
Timely Decision and Problem Solving(from the top management to operators)
Headquarters
Technical Service Center
・Problems happening at the site of operation
・Best practices of energy management
Refinery
Technical Service Staff
Refinery
Operation Groups
15
Enhancement of Competitiveness and Environmental
Preservation in Petrochemical Complex
Develop energy management practices from one refinery
to the whole petrochemical complex
Petroleum
Products
Petrochemical
Products
Catalysts
By-Products
Process Energy
Minimize
Environmental Load
Waste Material
Waste Heat
Petrochemical
Complex
Refinery
Maximize
Value of Products
Crude Oil
Naphtha
16
Cold Energy Utilization
at Chita
Environ. Impact
: Minimize
Cold Energy from Chita LNG’s Vaporization Plant
is introduced to Aichi refinery for process cooling
⇒ To improve cooling efficiency of the refinery
LNG
To reduce
sea water
intake.
Power Plant
Fuel
Vaporizer
×
Connecting
a Pipeline
To reduce
cold energy
discharge.
Reduced 40,000Kl of
crude oil throughput.
×
Crude
Oil
CDU
Residue Oil
RFCC
Power
Plant
Idemitsu Aichi Refinery
LPG
Recovery LPG
Propylene
Gasoline
Gas Oil
Idemitsu Aichi
Refinery
Chita
LNG
Chita LNG
Sea Water
Product Value
Add : Maximize
・Increase Recovery Ratio
of LPG and Propylene
・Increase Crackability
・Energy Conservation
Started operation in 2013
as one of the programs of RING’s
“Projects for Stable Supply of
Petroleum Products”17
RING:Research Association of Refinery Integration for Group-operation
Epilogue
Technology Management of Refineries for Future
- Keep up with the latest technology
- Build up operation technology and
know-how elaborately
- Balance between value of products and
impacts to environment
- Essential for the next generation refinery
18
Technology Exchange with Oil Producing Countries
Oil producing countries and Japan are good business partners into the future.
Idemitsu Kosan will promote technical exchange with oil producing countries
through the JCCP programs.
19
Thank you for your attention
20