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EMISSIONS FROM THE MANUFACTURING PROCESSES AND ON-SITE STEAM & POWER GENERATION
IN THE U.S. CHEMICAL INDUSTRYDr. Nesrin Ozalp
Assistant Professor of Mechanical EngineeringTEXAS A&M UNIVERSITY AT QATAR
Global Climate Change And Energy Project (GCEP) Workshop onCarbon Management in Manufacturing Industries
STANFORD UNIVERSITYStanford, CaliforniaApril 15 - 16, 2008
ENERGY CONSUMPTION vs. CO2 EMISSIONS IN THE U.S.
0
5000
10000
15000
20000
25000
30000
35000
40000
1972 1976 1980 1984 1988 1992 1996 2000 2004 2008
Industrial Transportation Residential Commercial
0
250
500
750
1000
1250
1500
1750
2000
1986 1988 1990 1992 1994 1996 1998 2000 2002 2004 2006
Transportation Industrial Residential Commercial
ENERGY CONSUMPTION AND CO2 EMISSIONS IN THE INDUSTRIAL SECTOR HAS BEEN LARGER THAN ANY OF THE OTHER SECTORS
OVER THE PAST THREE DECADES
ENERGY CONSUMPTION IN THE U.S. BY SECTOR, PJ CO2 EMISSIONS IN THE U.S. BY SECTOR, mmtCO2
Source: U.S. Energy Information Administration database: http://www.eia.doe.gov/environment.html
ENERGY CONSUMPTION vs. CO2 EMISSIONS BY SECTOR
0
50
100
150
200
250
300
350
1990 1992 1994 1996 1998 2000 2002
Petroleum and Coal Products Chemical ManufacturingFood Manufacturing Paper ManufacturingNon-metallic Manufacturing
CO2 EMISSIONS FROM MANUFACTURING, mmtCO2
Source: U.S. Energy Information Administration database: http://www.eia.doe.gov/emeu/mecs/mecs2002/data02/shelltables.html
ENERGY CONSUMPTION BY SECTOR, PJ
PETROLEUM AND CHEMICAL INDUSTRIES ARE THE LARGEST ENERGY CONSUMING AND CO2 EMITTING SECTORS
0
1000
2000
3000
4000
5000
6000
7000
8000
9000
1990 1992 1994 1996 1998 2000 2002
Petroleum and Coal Products Chemical ManufacturingFood Manufacturing Paper ManufacturingNon-metallic Manufacturing
THE CHEMICAL INDUSTRY IS CALLED
THE KEYSTONE IN THE U.S. ECONOMY
BECAUSE OF ITS CAPACITY TO
MANUFACTURE
MORE THAN 70,000 PRODUCTS
MAKING IT THE WORLD’S LARGEST
CHEMICALS MANUFACTURER
ENERGY CONSUMPTION vs. CO2 EMISSIONS IN THE U.S. CHEMICAL INDUSTRY
Coal, 300Other*, 475 LPG, 54
Residual Fuel Oil, 53
Natural Gas, 2093
250
260
270
280
290
300
310
320
330
1990 1991 1992 1993 1994 1995 1996 1997 1998 1999 2000 2001 2002
`
FUEL CONSUMPTION IN THE U.S. CHEMICAL INDUSTRY, PJ CO2 EMISSIONS IN THE U.S. CHEMICAL INDUSTRY, mmtCO2
Source: U.S. Energy Information Administration database: http://www.eia.doe.gov/environment.html
Share of total manufacturing emissions (%)
Aggregate CO2 Emission Coefficient (mmt per Quadrillion Btu of Energy Consumed)
% of [C] [C] / [E]
22.2 41.5
HOW CAN WE RELATE AND DESCRIBE THE CONNECTION IN ENERGY CONSUMPTION AND
CO2 EMISSIONS BY THE
MANUFACTURING PROCESSES,ON-SITE STEAM GENERATION
AND ON-SITE POWER GENERATION?
T E C H N O L O G I C A LE C O N O M I C A L P U B L I C P O L I C Y C H A N G E S
A COMPREHENSIVE DESCRIPTION OF INDUSTRIAL
ENERGY USAGE AND EMISSIONS PATTERNS CAN
PROVIDE INFORMATION ON THE POTENTIAL EFFECT OF
LET’S CHOOSE AN EXAMPLE
TO SEE THE COMPREHENSIVE
DESCRIPTION OF INDUSTRIAL ENERGY
USAGE AND EMISSIONS PATTERNS ON A
NATIONAL SCALE
HYDROGEN PRODUCTION IN THE CHEMICAL
INDUSTRY CAN BE CHARACTERIZED BY
CONSTRUCTING
MATERIAL, ENERGY AND EMISSION FLOWS MODELS
FOR THIS INDUSTRY
HYDROGEN IS AN “INDUSTRIAL GAS”
LET’S SEE WHICH SUBSECTORS OF THE
CHEMICAL INDUSTRY PRODUCES
“INDUSTRIAL GASES”
Source: U.S. Census Bureau, Current Industrial Reports: http://www.census.gov/industry/1/mq325c045.pdf
Industry Value % in total
Industrial Gas Manufacturing 4,791 92%
Plastics Material and Resin Manufacturing 162 3%
Other Basic Organic Chemical Manufacturing 135 3%
Petrochemicals 89 2%
Nitrogenous Fertilizer Manufacturing 26 <1%
TOTAL 5,203 100%
SUBSECTORS PRODUCING INDUSTRIAL GASES, M$
2003 2004Production Shipment Production Shipment
1.21x109 kg 8.43x108 kg 1.48x109 kg 1.14x109 kg
HYDROGEN PRODUCTION AND SHIPMENT BY THE CHEMICAL INDUSTRY
Source: U.S. Census Bureau, Current Industrial Reports: http://www.census.gov/industry/1/mq325c045.pdf
THE MAJOR HYDROGEN PRODUCTION
TECHNIQUE IN THE CHEMICAL INDUSTRY IS
THE STEAM REFORMING OF NATURAL GAS
Material Flow Model of Hydrogen Production
A MATERIAL FLOW MODEL REPRESENTS
MASS INPUTS AND OUTPUTSFOR AN INDUSTRIAL PROCESS.
IT IS CREATED BASED ON A MASS BALANCE FOR
EACH STEP OF AN INDUSTRIAL PROCESS.
Material Flow Model of Hydrogen Production
ONCE A MATERIAL FLOW FOR EACH PROCESS STEP IS CREATED FOR AN INDUSTRIAL PROCESS BASED ON UNIT MASS, THAT MATERIAL FLOW MODEL CAN BE SCALED AGAINST NATIONAL DATA BY USING
NATIONAL DATA ON PRODUCT OUTPUT.
THIS PROVIDES AN OVERALL NATIONAL PICTURE OF MATERIAL INPUTS AND OUTPUTS FOR AN INDUSTRIAL PROCESS.
Material Flow Model of Hydrogen Production
Source: Brown, H.L., Hamel, B.B., Hedman, B.A. (1996). Energy Analysis of 108 Industrial Processes. Fairmont Press, Atlanta, GA.
THE NEXT STEP IS
TO CHARACTERIZE THE ENERGY
CONSUMPTION OF THIS PROCESS,
SO THAT WE RELATE THIS
MANUFACTURING PROCESS WITH
ENERGY CONSUMPTION
TWO ENERGY FLOW MODELS ARE REQUIRED
TO ASSOCIATE MANUFACTURING
PROCESSES WITH ENERGY CONSUMPTION:
ENERGY END-USE MODEL
ENERGY PROCESS-STEP MODEL
GENERIC RELATIONSHIP BETWEEN ENERGY AND END-USES
PROCESS AND NON-PROCESS END-USES
CONSUME ENERGY IN THE FORM OF:
STEAM
FUEL
ELECTRICITY
WASTE HEAT
PROCESS END-USESPROCESS HEATINGPROCESS COOLING &
REFRIGERATIONMACHINE DRIVEELECTROCHEMICAL
PROCESSESOTHER
NON-PROCESS END-USESFACILITY HVACFACILITY LIGHTINGFACILITY SUPPORTONSITE TRANSPORTATIONOTHER
HOW TO DEVELOP AN ENERGY END-USE MODEL
THERE ARE 6 MODES OF POWER AND STEAM GENERATION IN THE CHEMICAL INDUSTRY:
1. INTERNAL COMBUSTION ENGINE WITH HEAT RECOVERY
2. GAS TURBINE WITH HEAT RECOVERY
3. STEAM TURBINE WITH HEAT RECOVERY
4. COMBINED CYCLE
5. STEAM GENERATION IN FUEL FIRED BOILER
6. STEAM GENERATION IN ELECTRIC BOILER
WHAT RELIABLE DATABASE PROVIDES THIS MUCH DETAILED
INFORMATION ON ENERGY CONSUMPTION FOR EACH INDUSTRY?
EIA 860B: ANNUAL ELECTRIC GENERATOR
REPORT FOR NON-UTILITY
Source: http://www.eia.doe.gov/cneaf/electricity/page/eia860b.html
Energy End-use Model of the U.S. Industrial Gas Manufacturing Sector, PJ1 1 7
0
2
1 1 9
B o ile r
P ro c e s s C o o l in g a n d R e f r ig e r a t io n
M a c h in e D r iv e
E le c t r o -C h e m ic a l P ro c e s s e s
O th e r P ro c e s s U s e
F a c i l i t y H V A C
F a c i l i t y L ig h t in g
F a c i l i t y S u p p o r t
O n s ite T ra n s p o r ta t io n
O th e r N o n -P ro c e s s U s e
N e t S te a m
N a tu ra l G a s
L iq u if ie d P e t ro le u m G a s
6 6
0
0
0
1
P ro c e s s H e a t in g
0
0
0
0
3 9
1
0
0
0
0
2 8
C o a l
C o k e a n d B re e z e
O th e r E n e rg y S o u rc e s E x c e p t
N e t S te a m
8
4
9
5
2 4
P u rc h a s e d E le c t r ic i ty
E le c t r ic ity S o ld
E le c t r ic ity f r o m N o n c o m b u s t ib le
R e n e w a b le s
O n s ite E le c t r ic ity G e n e ra t io n
0
2
U n re c o v e re d W a s te H e a t
W a s te H e a t
6
3 9 5 5
1 5
1 6
5 9
R e s id u a l F u e l O i l
D is t i l la te F u e l O il
0
0 0
0
2 7
0
3 3
4
1
0 3
2 3
10
1 1 1
0 0
0 2
0 2
3 0
0 0
0 0
0
1 1 9
7
5
D is t r ib u t io n L o s s e s 7
1
Source: Ozalp, N. PhD dissertation, University of Washington, 2005
FIRST,
THE KEY ENERGY CONSUMING PROCESS STEPSNEED TO BE IDENTIFIED.
THEN,
ENERGY USAGE IN EACH STEPSHOULD BE ALLOCATED AS “FUEL”, “STEAM”, “WASTE
HEAT” AND “ELECTRICTY”
HOW TO DEVELOP AN ENERGY PROCESS-STEP MODEL
THE KEY ENERGY CONSUMING PROCESS STEPSCAN BE IDENTIFIED BY REFERRING TO THE MATERIAL
FLOW MODEL.
ENERGY USAGE IN EACH STEPCAN BE ALLOCATED BY REFERRING TO THE ENERGY END-
USE MODEL
HOW TO DEVELOP AN ENERGY PROCESS-STEP MODEL
FUEL, STEAM, AND ELECTRICITY ALLOCATION AMONG END-USES
P ro cess H ea tin g
E lec tric ity
1
P ro cess C o o lin g an d
R efrig e ra tio n
M ach in e D riv e
E lec tro -C h e m ica l P ro cesses
O th e r P ro cess U se
F ac ility H V A C
F ac ility L ig h tin g
F ac ility S u p p o rt
O n site T ran sp o rta tio n
O th e r N o n -P ro cess U se
0
0
0
0
0
0
1 6
0
0
0
2
2
1
1
1 0 9
3
fu e l
s team
2310
0
0
7
0
0
0
0
2
0
0
0
Source: Ozalp, N. PhD dissertation, University of Washington, 2005
FUEL, STEAM AND ELECTRICITY
ALLOCATION GIVEN IN THE “PROCESS
END-USES” PART OF THE END-USE MODEL
NOW CAN BE ALLOCATED AMONG THE
PROCESS STEPS DESCRIBED IN THE
MATERIAL FLOW MODEL
Energy process-step Model of Hydrogen Production
Source: Ozalp, N. PhD dissertation, University of Washington, 2005
THE SAME METHODOLOGY CAN BE
APPLIED TO OTHER PRODUCTS OF
THE CHEMICAL INDUSTRY
TO CREATE SIMILAR
MATERIAL AND ENERGY FLOW MODELS
IF THE “REPRESENTATIVE PRODUCTION
TECHNIQUE AND THE PROCESS STEPS” ARE
CORRECTLY CHOSEN, THEN THE END-USE
MODEL AND THE PROCESS-STEP MODELS
RESULTS SHOULD BE IN AGREEMENT
LET’S SEE WHAT WE GET IF WE CREATE
ENERGY-PROCESS STEP MODELS FOR
ALL PRODUCTS OF THE INDUSTRIAL GAS
MANUFACTURING SECTOR
ENERGY END-USE DATA vs. ENERGY PROCESS-STEP MODEL DATA
Process-step
Model
Source: Ozalp, N. PhD dissertation, University of Washington, 2005
NOW LET’S COMPLETE RELATING
THE ENERGY USE AND THE EMISSIONS
IN THIS SECTOR BY GIVING
AN EMISSIONS FLOW MODEL
DEPICTING THE ENERGY CONSUMPTION AND
EMISSIONS FROM MANUFACTURING PROCESSES,
AND STEAM & POWER GENERATION
EMISSIONS FLOW MODEL OF THE INDUSTRIAL GAS MANUFACTURING SECTOR
Source: Ozalp, N. PhD dissertation, University of Washington, 2005
CONCLUSIONS
A COMPREHENSIVE AND CONSISTENT DESCRIPTION OF
CURRENT MANUFACTURING ENERGY AND MATERIAL
USAGE PATTERNS ALONG WITH EMISSIONS PATTERNS
CAN PROVIDE INFORMATION ON THE POTENTIAL
EFFECT OF TECHNOLOGICAL, ECONOMIC AND PUBLIC
POLICY CHANGES IN ENERGY INTENSIVE
MANUFACTURING SECTOR.
CONCLUSIONS
THEREFORE, IT IS IMPORTANT TO DEVELOP ENERGY,
MATERIAL AND EMISSIONS FLOW MODEL FOR MAJOR
ENERGY CONSUMING INDUSTRIES TO SEE THE
CHARACTERISTICS OF THE CORELATION BETWEEN
ENERGY CONSUMPTION AND EMISSIONS FROM THE
MANUFACTURING PROCESSES, AND STEAM & POWER
GENERATION.
WHAT WOULD BE
AN ALTERNATIVE PROCESS
TO AVOID OR REDUCE CO2 EMISSIONS
IN THE U.S. CHEMICAL INDUSTRY?
LET’S TAKE A LOOK AT OUR HYDROGEN
PRODUCTION EXAMPLE AGAIN TO SUGGEST AN
ALTERNATIVE PROCESS TO AVOID AND/OR
REDUCE CO2 EMISSIONS FROM
MANUFACTURING
CONCLUSIONS
UPGRADED CALORIFIC VALUE OF FUEL
NO CONTAMINATION OF PRODUCTIONS
AVOIDING OF IRREVERSIBILITIES RESULTING IN LOWER
THERMAL EFFICIENCY
NO DISCHARGE OF POLLUTANTS
THE U.S. CHEMICAL INDUSTRY WOULD HAVE THE FOLLOWING
ADVANTAGES IF IT CHANGES ITS CURRENT HYDROGEN
PRODUCTION PROCESS AND ON-SITE STEAM&POWER
GENERATION FROM TRADITIONAL INTERNAL/EXTERNAL
COMBUSTION TO SOLAR REFORMING/GASIFICATION :