In January of 2007, major energy de-regulation will take
place. This paper will discuss the changes and potential impacts on
the energy industry and end users. The UIC/ERC serves as the local
US Department of Energy Industrial Assessment Area through its center
of excellence, "The Energy Resource Center"
Over the years, the US Department of Energy has identified
many energy improvements with short payback periods with little to
no cost. The UIC Industrial Assessment Center will share its' considerable
experience serving as USDOE representative numerous industrial energy
audits and improvement projects. What to look for and how to make the
changes necessary to reduce energy consumption and improve the bottom
line.
| Mark Hamann |
10:15-11:15AM |
| ComEd/Exelon
Energy |
Successful Capital Projects: Our Electric
Utility's Eye
Look at energy Savings Case Studies |
As our premier provider of electric power and related
service, ComEd/Exelon will share its experience gleaned over the years
in developing and participating in numerous major industrial energy
projects. Case studies will illustrate specific projects and cost savings.
ABSTRACT:
You have identified the low hanging fruit and programmed major energy
capital expenses, but how do you keep energy improvement from being
a one-time "program of the year"? This presentation, by an international
energy consultant firm will describe their methodology to create
a permanent structure in management for continuous improvement in
plant energy utilization. Envinta is an international energy management
corporation specializing in top-level industrial management solutions.
BIO:
Chandan Rao is the President of Graphet Inc - an Energy Data Mining
and Analysis company. He has over 25 years of experience in energy
conservation for industrial process and institutional facilities
systems. Graphet Inc provides niche expertise for supporting sustainable
energy conservation, from energy management benchmarking, setting
of key performance indicators and accountabilities, to niche technical
expertise, implementation and tracking metrics that demonstrate results.
EnVinta & Graphet Inc have a strategic alliance to promote sustainable
processes for energy efficiency improvements. Mr Rao's expertise
is in facilitating energy teams and developing creative long-term
solutions for achieving sustainable energy conservation. He focuses
on a phased implementation approach, moving projects from concept
through implementation with accountability for results. He is experienced
in the evaluation and optimization of compressed air systems, industrial
ventilation systems and process cooling systems.
Choosing lighting is an activity rarely practiced by
plant engineers. However, light fixtures tend to have long lifetimes,
so the proper selection will have great effect on the bottom line.
This paper will examine advanced lighting fixtures, energy consumption,
aesthetic considerations and cost.
| Mark Hamann |
Track 1: 2:15-2:45PM |
| ComEd/Exelon
Energy |
Motors & Drives: Selecting and
Engineering Efficient Motor and Drives |
In industrial facilities, motor systems can account for
half to two thirds of the total electricity use. By implementing strategies
to replace inefficient motor designs with premium efficiency ones,
or installing variable speed drives to align system load versus motor
speed, energy consumption will be reduced. This presentation will provide
an overview on how to select the right motor and when variable speed
drives make sense. The presentation will also review motor management
practices and how procedural changes can yield substantial savings.
This presentation will address the process and equipment
associated with the generation and distribution of industrial plant
steam. The steam system fundamentals will be reviewed that highlight
areas where opportunities exist to improve steam system efficiency
and reduce operating cost.
This utility is often a set it and forget it item. Many
plants use air for valve operators, breathing, welding, etc. Leaks
and inefficiencies easily overlooked in otherwise functioning systems
add significant operational cost. This paper will look at design and
operational considerations as well as energy recovery options.
| Xin (Frank) Zhu and Keith Couch |
Track 1: 4:00-4:45PM |
| UOP LLC |
Combined Heat & Power Systems:
CHP and COGEN Global Overview |
Plant wide energy optimization requires integrating global
resources. This paper will look at tying together process and utility
energy sources and sinks to extract maximum value and cost effectiveness.
This will include co-generation as well as basic heat recovery. The
author will describe his "Pinch Technology" approach and energy hub
concept to assure global system energy optimization in real world plant
settings as applied by one of the worlds' largest developer and of
petroleum refining technology.
The best technical ideas and proposals remain only good
intentions when value is not effectively communicated to decision makers.
Understating and anticipating the criteria and concerns of financial
and managerial decision makers will improve the chances of success.
This presentation will tie everything together and take a serious but
light-hearted look at lessons learned from the perspective of these
two long time energy veterans.
| Michael Roberts, Joseph Rabovitser, Richard
Knight, Dmitri Boulanov, and Serguei Nester |
Track 2: 1:45-2:15PM |
| Gas
Technology Institute |
Illinois Coal Gasification/Reforming
Using Low-Temperature Plasma:
Research Opportunities in Stationary Power Generation and New Energy
Carriers |
A GTI led team is developing a novel gasification technology,
low-temperature Plasma Assisted Reforming (PAR), for co-production
of hydrogen, syngas, substitute natural gas (SNG) and electricity from
coal. In the PAR process, micronized coal is converted to product gas
at temperatures of 500 to 700°C. The product gas is fed into a
warm gas cleanup unit for removal of sulfur, mercury and other contaminants
and then into a purification unit for gas separation and CO2 capture.
Based on GTI’s proof-of-concept studies (already conducted),
PAR can exceed performance targets of traditional high-temperature
gasification for efficiency, costs, and emissions.
In a Phase I project funded by ICCI in 2005, GTI started evaluation
of the suitability of the PAR process for low-temperature gasification
of Illinois coal for four prospective applications: production of hydrogen,
fuel gas for gas turbines, syngas for Fisher-Tropsch synthesis, and
SNG for natural gas markets. Two Dielectric Barrier Discharge (DBD)
plasma test units located at GTI’s Combustion Lab in Des Plaines,
IL are being utilized in the project. A laboratory scale semi-batch
200-W DBD reactor is used for characterization of the coal reactivity
in a fixed bed arrangement. Scale up studies in a continuous flow pilot
scale 3-kW DBD reactor focus on process optimization, and economic
and environmental evaluation. A system analysis is being conducted
to identify projected markets for Illinois coal, to prepare a process
database and to develop a technology plan. Experimental data collected
to date indicate the technical feasibility of the PAR-based gasification
of Illinois coal. Preliminary modeling results show a 25% cost reduction
and at least 10% efficiency increase of the PAR technology compared
to traditional gasification.
Based on Phase I proof-of-feasibility results, the Team plans to initiate
Phase II development of the PAR technology for Illinois coal: to conduct
process characterization studies and produce PAR operation parameters
for scale up of the technology to the MW-scale pilot level. The goal
of the Phase II effort is to characterize and optimize the PAR-based
gasification of Illinois coal for four prospective markets: hydrogen,
fuel gas, syngas, and SNG. The effort will include: (1) Evaluation
and selection of required process parameters for four applications;
(2) Experimental study of coal preparation for the PAR process; (3)
Development of the BDB gasifier; (4) Experimental study of the PAR
in a DBD gasifier; and (5) Development of detailed specifications for
a Phase III MW-scale pilot plant.
| John Aycock, Senior Engineering Associate |
Track 2: 2:15-2:45PM |
| Eastman
Chemical Company |
| Chemicals and Power Co-Production by
Gasification of Illinois Coal |
The U.S. chemical industry is highly dependent on raw
materials derived from petroleum or natural gas. Escalating prices
and increased volatility in recent years have magnified the risk of
this lack of raw material diversification. Coal has the potential to
be a primary source of energy as well as a feedstock for chemicals
due to its abundance of supply, relatively low cost and relatively
low price volatility as compared to other fossil fuels. As a result,
Eastman Gasification Services Company conducted a study for the Illinois
Clean Coal Institute to evaluate the feasibility of chemicals production
from Illinois coals and help lay the groundwork for chemicals project
development in the State of Illinois. Two main process options were
evaluated in the course of this work: standalone coal to chemicals
based on gasification and syngas processing; and coproduction of chemicals
from coal in combination with Integrated Gasification Combined Cycle
for power production. Though this review focuses predominantly on methanol
(MeOH) as a representative chemical product, in that MeOH is highly
versatile with a variety of uses in manufacturing and energy applications,
the results can be extrapolated to a number of additional chemicals
that may be particularly advantageous to Illinois. All major areas
that impact the economic and technical feasibility of a potential coal-to-chemicals
project at an Illinois mine mouth site were evaluated including the
characteristics and suitability of Illinois coals; marketing issues
for chemicals, power, and Illinois coal; optimum process design and
configuration; capital and operating costs of each mode of production;
and impact of financial structure and assumptions.
Bruce G. Bryan, P. Vann Bush, Rachid B. Slimane,
Larry G. Felix, and Michael Roberts |
Track 2: 2:45-3:15PM |
| Gasification & Gas Processing Center, Gas
Technology Institute (GTI) |
GTI’s Flex-Fuel Test Facility – An
Overview of Recent and Ongoing Projects and Accomplishments
PRESENTATION SLIDES |
To support the development and commercialization of its
gasification technologies and provide a cost-effective platform for
evaluating emerging syngas end-use applications, GTI has designed,
constructed, and commissioned a state-of-the-art pilot-scale gasification
facility, the Henry R. Linden Flex-Fuel Test Facility. Built with support
from the natural gas industry and the State of Illinois, the test facility
was successfully commissioned in early 2004 and has since been used
in the performance of three projects. The first project focused on
the evaluation of the gasification characteristics of a high-ash Indian
coal with the goal of qualifying this fuel as a suitable candidate
for IGCC. The second project involved feasibility demonstration tests
of the Novel Gas Cleaning “filter-reactor” Process, a syngas
ultra-cleaning technology that is being developed jointly with Siemens
Power Generation. The NGC Process concept turns barrier filters into
chemical reactors when they collect fine sorbent particles injected
into the syngas stream. A NGC Process section, comprising two Siemens
barrier filters, three sorbent injection systems, a bulk sulfur removal
system, and other equipment, was designed, integrated with the facility,
and operated. The facility was also fitted with innovative sample extraction
and conditioning systems and state-of-the-art instrumentation that
enable comprehensive, real-time assessment of NGC Process performance
with syngas derived from gasification of three different coals, including
a North Dakota Lignite. In the third project, the gasifier was operated
as a fluid-bed biomass gasifier with pelletized wood to evaluate the
tar-cracking ability of alumina and sintered olivine bed materials
and establish tar-cracking performance benchmarks for comparison with
a new class of catalytically-active bed materials under development
at GTI. The real-time sampling systems in place at the facility were
used to assess the tar-cracking performance of these bed materials.
The capabilities of the Flex-Fuel facility are continually being expanded.
In one ongoing project, a pilot-scale gas/liquid contactor is being
relocated from Texas and will be integrated into the facility for conducting
conventional syngas cleanup and CO2 capture research based on the Morphysorb® physical
solvent technology for upgrading subquality natural gas, which has
been commercialized by GTI and Uhde. In another project, GTI is beginning
work with Headwaters Technology Innovation (HTI) Group, Inc. in pilot-scale
testing of HTI’s iron-based catalysts for the production of high-hydrogen
content Fischer-Tropsch (FT) liquid products. In another effort, GTI
is a key participant in the Pratt & Whitney Rocketdyne/DOE advanced
single-stage gasifier development program for high-efficiency and low-cost
production of synthesis gas. A pilot-scale version of PWR’s advanced
coal gasifier will be installed and operated at GTI, with significant
additions to the facility including advanced coal feeding and gas cooling
systems, a high-pressure oxygen supply system, and a hot gas filter
fines lockhopper discharge system. An overview of these recent and
ongoing activities will be provided in this paper, with a focus on
results and accomplishments.
The Illinois State Geological Survey (ISGS) has been
investigating the potential for carbon sequestration in the Illinois
Basin since October 2003. Results to date have shown the geology to
be potentially suitable for carbon dioxide (CO2) storage, and a series
of pilot tests is now underway. While this work has been in progress,
the ISGS also provided the geological and carbon sequestration reservoir
analysis for the proposals that netted Illinois two of the four semifinal
sites being considered for the FutureGen power plant project, as announced
by the U.S. Department of Energy and the FutureGen Industrial Alliance
on July 25, 2006. The sites are located near Tuscola and Mattoon, Illinois.
Seven states offered twelve sites in the first round of the competition;
the other two semifinal sites are in Texas. ISGS researchers have defined
the geology and engineering characteristics of the subsurface reservoirs
that could handle up to 1 million metric tons of CO2 per year over
the life of a FutureGen facility, defined the seismic stability of
potential sites, helped define pipeline corridors potentially needed
to move the CO2, and provided base maps and aerial photographs of the
sites to support site evaluation. In addition, ISGS staff attended
public meetings in these communities to explain CO2 sequestration and
helped to explain the entire project to the public, as well as to increase
awareness of the role of greenhouse gases like CO2 and the potential
for climate change. Regardless of the outcome of the FutureGen competition,
the Illinois Basin remains a prime area for coal gasification project
development both because of the coal resources available and because
of the suitability of the geologic framework for carbon sequestration.
Several resources could be used to produce the hydrogen. Leading
contenders include fossil, renewable, and nuclear energy. Of
course, a combination of these sources is a more likely supply scenario. Each
of these routes creates a new set of technical and regulatory challenges.
At present in the U.S., the resource chain for producing
hydrogen starts with petroleum products, such as natural gas or naphtha.
These feedstocks are converted to hydrogen and carbon dioxide by means
of a process called catalytic reforming. Variations on the basic reforming
process account for 96 percent of all hydrogen produced today. Worldwide,
63 percent of the hydrogen produced is used for manufacturing ammonia
fertilizers, with the remainder used principally in refineries to remove
sulfur and nitrogen pollutants from gasoline, diesel, and jet fuel. The
possibility of using hydrogen for automotive transport has been a focus
of DOE programs since the "FreedomCar Partnership" was announced in
2002 followed by President Bush's announcement of a hydrogen initiative
in the State of the Union Address in 2003. Most near-term hydrogen
production will likely continue to be made from natural gas reforming
because this is a low-capital investment route.
Carbon dioxide capture technologies combined with Shell
integrated gasification combined-cycle (IGCC) power systems producing
both hydrogen and electricity could operate on high-sulfur Illinois
coals and should be considered. The economics of large scale
coal-to-hydrogen look favorable as the current prices for natural gas
remain the norm. Comparisons of energy penalties, capital
investment, and CO2 emission reductions
based on the full energy cycle - including mining, coal transportation,
coal preparation, gasification, gas treatment, power generation, infrastructure
to transfer power or hydrogen to end users, and pipeline transport
of CO2 for sequestration are reasonably
certain for the coal route and will be presented. The technical aspects
of H2 pipelines and supercritical CO2 pipelines,
as well as issues relating to CO2 sequestration
in a variety of host reservoirs, will be considered. The largest challenges
will be the transport of carbon dioxide and the availability of carbon
dioxide sequestration reservoirs. Here the regulatory landscape
is still not fully formed.
Emerging technologies for hydrogen production linked
to a revitalized nuclear industry using Gen-III+ and high-temperature
Gen-IV reactors will also be considered. For the nuclear cases,
commercial electrolysis provides a benchmark against which research
on thermochemical cycles and high-temperature steam electrolysis must
be measured. Even the most-promising of these nuclear routes
has not yet been demonstrated at the integrated process scale yet,
although this work is on track.
Biodiesel is now well accepted as a legitimate, diesel
fuel alternative offering multiple advantages over petroleum such as
renew-ability, energy security, and superior environmental performance.
Additionally, the growth of a biodiesel industry can catalyze rural
economic development through value-addition and establishment of processing
centers. This has spurred many states in the U.S. to promote the use
of biodiesel.
In addition to virgin vegetable oil, by-products from vegetable oil
processing have attracted attention as a potential feedstock for biodiesel
manufacture. Waste grease is collected from grease traps installed
in commercial, industrial or municipal sewage facilities that separate
grease and oil from wastewater. Commercial vegetable oil producers
produce millions of gallons of waste grease annually. However, this
type of grease contains a significant amount of water and other contaminants
and is considered of very low quality with little monetary value. Some
of the grease is used in animal feed but most of it tends to be disposed
of as waste.
This presentation will discuss how the Illinois Waste Management and
Research Center (WMRC) has converted various vegetable oil by-products
to biodiesel and assisted other entities in the conversion. WMRC has
worked with large-scale vegetable oil processors to develop a biodiesel
conversion process for the oily by-products. Additionally, WMRC has
assisted a variety of Illinois interests to convert by-products to
biodiesel resulting in reduced waste and fuel cost. Specifically, WMRC
has provided assistance a High School (they used biodiesel produced
from their rancid cafeteria grease to power a bus), a bussing company,
a State agency, a farmer, a landscaping firm and a variety of private
citizens.