Legislature(2011 - 2012)
04/15/2011 02:20 PM House RES
| Audio | Topic |
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| Start | |
| Presentation(s): Gigamethanol and Gas to Gasoline | |
| Adjourn |
* first hearing in first committee of referral
+ teleconferenced
= bill was previously heard/scheduled
+ teleconferenced
= bill was previously heard/scheduled
ALASKA STATE LEGISLATURE
HOUSE RESOURCES STANDING COMMITTEE
April 15, 2011
2:20 p.m.
MEMBERS PRESENT
Representative Eric Feige, Co-Chair
Representative Paul Seaton, Co-Chair
Representative Peggy Wilson, Vice Chair
Representative Alan Dick
Representative Neal Foster
Representative Cathy Engstrom Munoz
MEMBERS ABSENT
Representative Bob Herron
Representative Berta Gardner
Representative Scott Kawasaki
OTHER LEGISLATORS PRESENT
Senator Thomas Wagoner
COMMITTEE CALENDAR
PRESENTATION(S): GIGAMETHANOL AND GAS TO GASOLINE
- HEARD
PREVIOUS COMMITTEE ACTION
No previous action to report
WITNESS REGISTER
THOMAS P. ROCHE
T.P. Roche Company
Kemah, Texas
POSITION STATEMENT: Testified during the discussion of
GigaMethanol and Gas to Gasoline presentation.
DEO VAN WIJK, Chairman
Janus Methanol Ltd.
Porter, Texas
POSITION STATEMENT: Testified during the discussion of
GigaMethanol and Gas to Gasoline presentation.
CHARLES SINK, Director of Enterprise & Trust Services
Chugachmiut
Anchorage, Alaska
POSITION STATEMENT: Testified during the discussion of the
GigaMethanol and Gas to Gasoline presentation.
SENATOR TOM WAGONER
Alaska State Legislature
Juneau, Alaska
POSITION STATEMENT: Testified during the discussion of the
presentation on GigaMethanol and Gas to Gasoline.
ACTION NARRATIVE
2:20:50 PM
CO-CHAIR PAUL SEATON called the House Resources Standing
Committee meeting to order at 2:20 p.m. Representatives Seaton,
Feige, Foster, Dick, P. Wilson were present at the call to
order. Representative Munoz arrived as the meeting was in
progress.
^PRESENTATION(S): GigaMethanol and Gas to Gasoline
PRESENTATION(S): GigaMethanol and Gas to Gasoline
2:21:06 PM
CO-CHAIR SEATON announced that the only order of business would
be a presentation on GigaMethanol and Gas to Gasoline.
A brief at-ease was taken.
2:23:34 PM
THOMAS P. ROCHE, T.P. Roche Company, introduced himself.
2:23:43 PM
DEO VAN WIJK, Chairman, Janus Methanol Ltd., related that he has
built eight methanol plants around the world. Of the last
three, two are mentioned in the presentation, including in
Frankfurt.
2:24:16 PM
CHARLES SINK, Director of Enterprise & Trust Services,
Chugachmiut, stated that Chugachmiut is a regional non-profit
for the Chugach Region. He said he persuaded Mr. van Wijk to
come to Alaska to do a scoping of his technology and explain how
it would fit in Alaska.
2:24:52 PM
MR. VAN WIJK indicated this presentation was prepared and given
during the National Petroleum Refinery Association (NPRA) in San
Antonio in March 2011. Janus Methanol AG, a Swiss-based company
has offices in Germany, the Netherlands, Porter, Texas, and his
role is as Chair of the company [slide 2].
2:25:10 PM
MR. VAN WIJK stated that the company has been considering at
complexes in the Netherland, Russia, Mozambique, Texas, and
possibly Alaska. The project needs is huge volumes of natural
gas, minimum of capacity of 640 million or two-thirds of a bcf
of natural gas [slide 3].
2:25:59 PM
MR. VAN WIJK stated that his company worked with British
Petroleum (BP) to develop the plants in Trinidad and Tobago. He
explained that having one of the major oil and gas producers
involved immediately makes the project viable. He further
stated that his company is one of the smaller companies so being
creative and at the forefront of technology is important to
convince larger companies that the company brings something
special to the projects. Thus far Janus Methanol AG has been
successful in doing so. His group has collectively in excess of
500 years of methanol experience. No other group has ever had
that much experience to offer [slide 4].
2:26:40 PM
MR. VAN WIJK turned to the 2009 photograph of Trinidad and
Tobago, noting that in 1984 this space was empty sugar cane
country [slide 5]. Today, about $15 billion has been invested
in the country, thousands of people find employment. He
suggested people can learn from their mistakes, noting the
photograph shows a hodgepodge of industries, including ammonia,
methanol, and steel industries. No one thought through the
design, but the area has been very successful in attracting
industry.
2:28:05 PM
MR. VAN WIJK explained that Janus Methanol AG was the first
company to build a 5,000 tons methanol plant in Trinidad and
Tobago using the MegaMethanol technology [slide 7]. Thus far,
six plants have been built. He said that due to financial
reasons he sold his company Saturn to a large corporation,
Methanex. He was then absent from the business for ten years,
during which time Methanex developed the technology going from
5,000 to 10,000 tons of methanol per day. The plants are built
in clusters of two, so 20,000 tons of methanol per day or 7
million tons of methanol per year. He identified one problem,
which is that the chemical market for methanol is 31 to 32 tons
million per year and including China the market totals 46
million tons per year. He offered that if a company built four
clusters of plants it would dominate the world of methanol, but
producing such a large amount of methanol would ultimately
reduce the price of methanol [slide 7].
2:29:33 PM
MR. VAN WIJK related he attended a conference in Russia where
ExxonMobil Corporation unveiled its methanol to gasoline
technology (MTG). ExxonMobil Corporation's first plant was
built in New Zealand in 1982. He reminded members of the 1979
oil crisis and surmised that New Zealand feared being left out
so it developed the methanol to gasoline technology (MTG). The
technology was technically success but commercially in the 1990s
oil prices fell to $10 per barrel and ultimately the project
failed. Exxon bought Mobil and the technology was forgotten, he
said. He related that China has built an MTG plant based on
coal, noting all petrochemical projects in China are based on
coal. However, one disadvantage of coal is the expense. He
pointed out that it is much cheaper to use natural gas in the
MTG process [slides 8 and 9].
2:31:03 PM
MR. VAN WIJK turned to the photographs of the ATLAS plant in
Trinidad [slide 10-11]. In 2008, it was the best performing
plant ever built. He identified the components of the plant,
including the distillation, fired heater, syngas compressor,
syngas generation, and methanol synthesis. The engineers
determined the best place to save costs would be in the syngas
generation plant. He said the steam reformer represents about
20 to 25 percent of the total investment but the costs for the
syngas compressor alone is 25 million euros (¼ , yet the syngas
compressor has been very vulnerable to breakdown.
2:32:36 PM
MR. VAN WIJK said the engineers at Janus Methanol AG worked to
skip the steam reformer, which in 2004 deemed unnecessary to
methanol gas production [slide 12]. He identified that the
right one is gas cooled and the left one is water cooled [slide
13]. The advantage bypassing the syngas compressor and not
needing the huge compressor only three vessels would be required
to produce a total of 10,000 tons of methanol per day.
2:33:37 PM
MR. VAN WIJK stated one additional advantage has been gained
during distillation using this method since the steam reformer
could only run at 40 to 44 bars but the new method can run at 60
bars. The same size of plant could produce double the volume
[slide 14]. Mr. van Wijk stated that the syngas compressor is
gone in this photograph [slide 15]. Instead of the 25 million
(¼ cost for the syngas compressor, the booster only costs 4
million euros (¼ . This process also changed the fired heater
and sea water cooling system, but the one depicted is a much
larger system than would be necessary in the Gulf of Alaska
[slides 16 and 17].
2:34:55 PM
MR. VAN WIJK summarized that Janus Methanol AG has been able to
reduce the cost of the per ton annual capacity [slide 18]. He
predicted that if a 3,000 ton methanol plan was built today it
would cost $1,000 per ton of annual installed capacity or about
$1 billion in total. However, the ATLAS plan would cost $600
per ton of annual installed capacity. He predicted that taking
steps to increase production to 20,000 tons per day (tpd) using
this technology would reduce the cost to $300 per ton. Thus, a
total of 7 million tons of methanol could be produced annually
for about a $2 billion investment. In response to a question,
he answered that these costs are in dollars.
2:36:19 PM
MR. VAN WIJK stated Janus Methanol AG already has a big plant
but it would like to build more plants. He outlined the known
methanol conversion technologies as methanol to gasoline (MTG),
methanol to Propylene (MTP), and methanol to olefins (MTO), but
that in his view the MTP and MTO are technically proven but not
commercially proven [slide 20].
2:36:59 PM
MR. VAN WIJK pointed out the plant photograph in New Zealand and
the process it uses [slides 22 -25]. He turned to the world's
first coal to liquids plant using MGT in Shanxi Province in
China [slide 26].
2:37:18 PM
MR. VAN WIJK reported the specifications of MTG gasoline
properties and composition which is high in octane at 92 percent
without producing any sulfur [slide 27]. He related two
products are produced in the Janus Methanol AG plants. Out of 7
million tons of methanol, three million tons of gasoline and 4
million tons of water are produced. The water byproduct is pure
enough that it could be used for cooling purposes or
agriculture. Additionally, the MTG yields meet all U.S.
specifications, he said.
2:38:30 PM
MR. VAN WIJK stated one important aspect is that all of the
majors have investigated billions on gas-to-liquids using the
Fischer Tropsch method. That process produces fuel, LPG,
naphtha, distillate/diesel, but also a large amount of wax. The
MTG route produces some LPG, but yields approximately 89 percent
of gasoline [slide 29]. The process does not produce any other
byproducts except water and meets all U.S. specifications. In
response to Co-Chair Feige, he agreed the two columns
represented the outcome using cobalt and iron catalysts.
2:40:06 PM
MR. VAN WIJK, in response to a question, agreed that the
temperatures listed as 220 C and 340 C refer to the centigrade
temperatures used.
CO-CHAIR SEATON inquired as to the temperature that the MTG
process uses.
MR. VAN WIJK answered that the methanol pod runs at a
temperature of 1200 degrees centigrade (C) for syngas. The
gasoline pod uses a substantially lower temperature. He
described several steps necessary: first methanol is made, which
contains 56 percent water; next the water would be separated
through a small-dimethyl ether (DME) plant; and finally, the
methanol would be converted by using the methanol to gasoline
(MTG) process.
2:41:04 PM
MR. VAN WIJK provided liquid transportation fuels from coal and
biomass figures from ExxonMobil [slide 30]. He estimated the
cost to build a Gulf Coast plant at $2.6 billion, including the
cost of the methanol, DME, and MTG plants.
2:42:07 PM
CO-CHAIR SEATON asked whether the $2.6 billion is for the MTG
with carbon capture or without carbon capture.
MR. VAN WIJK answered that the cost estimate included carbon
capture.
CO-CHAIR SEATON related his understanding that would result in
20,000 tons of methane per day.
MR. VAN WIJK agreed, noting it would result in about 8,600 tons
or 63,000 barrels of gasoline per day.
CO-CHAIR FEIGE presumed the carbon dioxide would be reinjected.
MR. VAN WIJK agreed.
2:43:03 PM
MR. VAN WIJK turned to the last slide that illustrates the
proposed plan for a plant in Mozambique [slide 31]. He said he
was unsure this would be suitable for Alaska. He pointed out
the right side of the slide depicts two methanol plants with the
total capacity of 10,000 tons and on the left side. The plan
would be to build two ammonia plants with the capacity of 7,500
tons each. He related the whole range of downstream products
made partly based on methanol and partly based on ammonia,
including formaldehyde and gasoline. He characterized
Mozambique as the fifth poorest country in the world with a
population of 23,500,000 and a life expectancy of 37 years of
age. Only 350,000 people have jobs, and of those 150,000 are
government jobs. He identified this complex as a C1
petrochemical complex, which would consist of 25 plants. The
workforce needed would encompass between 40,000 and 50,000
people on site. The amount of land needed is huge, but little
else exists in Mozambique. He predicted the plant would need a
community of about 300,000-350,000 people in size to support it.
2:45:58 PM
MR. VAN WIJK passed out a handout which compared North Slope
costs to Gulf Coast costs. He acknowledged that he has little
knowledge of North Slope construction costs so he made some
broad assumptions. He estimated the total project cost at $5.2
billion, with depreciation over 15 years, which would equate to
a cost of $116 per ton. He calculated the return on investment
at 20 percent after tax, which "boils down" to a return of $347
per ton. He provided estimates and cost per ton on items,
including a 35 percent tax estimate of gross revenues or $186
per ton the oxygen plant at double the cost or $84 per ton, an
estimated 225 employees for actual operation, and 2,500 to 3,000
employees during construction. He estimated $150,000 person for
wage or $11.25 per metric ton of gasoline and operating expenses
at $50 million or $49.50 per ton and the catalyst cost per ton
at $15.25.
2:48:13 PM
MR. VAN WIJK estimated total operation expenses based on a per
ton cost of gasoline of $810, noting this estimate includes a
gross margin of $533 per ton. He said gasoline equals 367
gallons per metric ton. He estimated the natural gas feedstock
cost at $2.00 per MCF or $160.00 per metric ton, which equates
to $2.20 per gallon excluding the natural gas. Adding the cost
of natural gas would bring the total feedstock cost to $2.64 per
ton, which includes a profit of $1.45, he said. The real cost
of 2.00 MM/BTU would be $1.20, including depreciation, he added.
2:50:22 PM
MR. VAN WIJK pointed out that an argument could be made over the
profit margin and while he was unsure what it should be he
believed it would depend on market value. He summarized that
the potential to produce gasoline, even by doubling construction
costs of $2.65 to $2.85 would allow a $1.45 per gallon margin.
He compared that to today's wholesale prices which are in excess
of $3 per gallon so the margin would increase to about $2.00 per
gallon at today's prices.
2:51:40 PM
MR. VAN WIJK speculated as to how this is possible. He said 80
percent of the investment is for the methanol component and 20
percent for the production cost of DME gasoline. He
acknowledged that the costs are extremely sensitive at the front
end, but once those are under control, the rest would follow.
2:52:23 PM
MR. VAN WIJK recalled the proposed estimate in Alaska is that an
estimated at 4.5 bcf of gas would be available on the North
Slope which represents the equivalent of 14 plants with the
capacity in methanol of 1.12 million barrels per day. He stated
that another advantage of methanol is that it can be blended
with oil and it still keeps the oil fluid. He has heard wide
ranging estimates, in terms of the Trans-Alaska Pipeline System,
anywhere from 2 MMbbl to 4 MMbbl per day. Currently, he thought
the volume produced was 640,000 barrels per day. He outlined
problems encountered with low volumes of oil including viscosity
issues unless methanol or gasoline is injected. He said this
problem exists in Siberia, where lots of oil that cannot be
moved because it freezes up. However, that does not happen when
the methanol is added, he said.
2:54:19 PM
MR. VAN WIJK related that the plan would be to ship the
oil/methanol slurry to Valdez, distill the methanol out, and
then ship the gasoline to Japan and other countries in the Far
East. The Far East is the likely market due to the restrictions
and costs of the Jones Act. He predicted that if producers were
forced to sell to California the gas price would be lower than
if it is shipped to the free market. He surmised that Alaskans
must be unhappy with the Jones Act since it costs them money.
2:55:36 PM
MR. ROCHE suggested further discussion on the potential with the
4.5 bcf per day design basis for use with the TransCanada
pipeline. He estimated that if that gas was used for this
application, it would mean 14 trains instead of 2 trains, so the
investment would be spread over 15 years and could fully use the
TAPS.
2:56:11 PM
MR. VAN WIJK agreed. He estimated 1,500 people would be need in
7 complexes and a construction force of about 3,000 people for
about 15 to 18 years. He predicted the plants would produce
about 140,000 tons of methanol per day or 450,000 barrels of
gasoline per day. He offered his belief that this would change
the low-priced gas into a huge money maker. He compared that to
exporting natural gas to the Lower 48 since he predicted that
natural gas would remain in the next 10 to 15 years at $4 to $6
per million. A variety of possibilities for using natural gas
exists, such as to produce gasoline or develop a C1 chemical
complex. These are tools currently available and are
technically proven, but the North Slope is not an easy climate
to build in. However, the pipeline has already been built so it
made sense to him to use the TAPS for delivery, he said.
2:59:09 PM
MR. VAN WIJK offered his belief often the best solutions are the
simplest solutions. He said he found this solution by pure
accident. He detailed several other meetings he has attended and
concluded that this technology is promising and will change
geopolitical, geoeconomical, and geosocial aspects worldwide.
He concluded that the U.S. has tremendous potential to increase
gasoline production and eliminate its overall debt. He
estimated that the first plant could be online in in five years.
3:02:40 PM
SENATOR TOM WAGONER, Alaska State Legislature, asked him to
repeat the one formula for conversion and whether it pertained
to 450,000 gallons or barrels.
MR. VAN WIJK answered barrels. In further response to Senator
Wagoner, he said he used 140,000 tons per day.
CO-CHAIR SEATON wanted to be certain to get the comments on the
record.
SENATOR WAGONER reiterated his question was on the conversion
from the 140,000 tons per day throughput on the estimated
maximum number of trains to 450,000 barrels per day.
3:04:01 PM
MR. VAN WIJK, in response to a question, answered that the oil
would most likely be blended because of the importance in
keeping the oil fluid. He detailed that he envisioned a total
of 14 trains, with each train consuming 320,000 BTU. However,
noting his preference in building tanks in pairs so the total
consumption would be 640,000 BTU. Fourteen trains could produce
up to 140,000 tons of methanol per day, which converted to
barrels would equal 1.12 MMbbls of methanol per day. The yield
would be 43 percent, since methanol contains 56 percent water,
which would result in a production of about 450,000 barrels of
gasoline per day. He characterized the proposed project as "one
heck of a refinery." He reported that a world-scale refinery
would produce 200,000 barrels per day and would cost at least
$10 billion to build, if a permit could be had. He related his
understanding that a permit for a refinery has not been issued
for more than 25 years. He offered his belief that the proposed
project as described would be "permittable."
3:06:03 PM
SENATOR WAGONER inquired as to whether the water used would be
pure enough that it could be used for hydro-fracking.
MR. VAN WIJK answered absolutely. He said it is so pure it
would be drinkable. He explained that Janus Methanol AG will
build ammonia and urea plants in Africa, but that the continent
has a shortage of available water so any byproduct water would
be used for irrigation.
3:07:21 PM
MR. VAN WIJK distributed a handout of his calculations to
committee members labeled "A" and "B."
3:07:37 PM
REPRESENTATIVE P. WILSON asked the reason that the jobs stop at
15 years.
MR. VAN WIJK reviewed the employees for construction and
operation. About 1,500 employees would be needed indefinitely
to run the plant. Approximately 3,000 construction jobs would
disappear after construction but construction would last between
15 and 20 years. He acknowledged he does not have experience
building on the North Slope, but normal construction time for a
project of this size is 36 months and it would take another two
years to obtain financing, he said.
3:08:56 PM
MR. SINK clarified that Mr. van Wijk's projections are for the
proposed two-train plant.
MR. VAN WIJK explained that the output would be 640 million per
day, with $300 per gallon capacity based on the Gulf Coast
model. In response to Co-Chair Seaton, he agreed the figures
are based on a proposed two-train Atlas-sized plant.
MR. VAN WIJK clarified for Representative Munoz that he just
doubled the capital costs. He referred to his handout, labeled
"A" and the figure of $810, which contains $533 per ton gross
profit, of which 35 percent represents taxes. He estimated $558
million in taxes, not counting and production royalty costs.
3:10:39 PM
CO-CHAIR SEATON inquired as to whether the calculations have
been made.
MR. VAN WIJK answered yes.
3:10:50 PM
CO-CHAIR SEATON reviewed his calculations. He referred to the
handout previously referenced to the second line down which
projects the return on investment of 20 percent at $2.6 billion,
and tax at 35 percent.
MR. VAN WIJK said he doubled the oxygen cost and adjusted the
labor to $150,000 per person, increased the operating costs to
$100 million, and added in the catalyst's cost. He divided the
total of $810 by 367 and arrived at a total cost of $2.21 per
gallon excluding natural gas.
3:11:55 PM
MR. VAN WIJK reviewed his figures on chart "B" again. He
related that 367 gallons per metric ton using 80 MM/BTU would be
required to produce 1 gallon of gasoline. He said that he added
$.436 per gallon to the $2.21 for a total of $2.64, which
includes $1.45 gross margin less the 35 percent taxes. He
concluded the real cost would be $1.20 per gallon based on a
$5.2 billion investment.
3:12:55 PM
REPRESENTATIVE FOSTER asked for an explanation of a train.
MR. VAN WIJK returned to slide 11 and identified a train.
3:14:27 PM
REPRESENTATIVE FOSTER asked for involvement of Chugachmiut in
the project.
MR. SINK answered that his involvement has been loosely based on
my acquaintance with Mr. Roche. He brought Mr. van Wijk to
Alaska and he serves as his contact in Alaska. He offered that
Chugachmiut is a Native non-profit serving health and social
services. His division has the Village Protection Safety
Program, but he also deals with real estate and forestry, as
well as economic and business development for individual tribes.
3:16:22 PM
MR. SINK related that Chugachmiut been working on the quality
and sustainability of jobs, which is a topic he has discussed
with Mr. van Wijk.
CO-CHAIR SEATON commented two villages are in his region.
MR. VAN WIJK said it has always been his philosophy to train and
use as much local personnel as possible on projects.
3:17:21 PM
SENATOR WAGONER asked how many acres each train would require.
MR. VAN WIJK responded that each train uses approximately 40
acres, which includes the tank farm.
3:17:44 PM
MR. VAN WIJK referred to slide 11 and pointed out the various
tanks.
CO-CHAIR SEATON inquired as to whether methanol is commonly
known as wood alcohol.
MR. VAN WIJK answered he is correct. He provided a brief
history, noting that window washing fluid is 50 percent
methanol. In the 1980s California tried to introduce M85, a
blend of 85 percent methanol with 15 percent unleaded premium
gasoline, and M100, which is pure methanol. He anecdotally
stated that "big oil" did not like that effort. He reported
that methanol is used to produce 4 percent of the products made
in the U.S., including nylon, formaldehyde, and glue.
3:20:47 PM
MR. VAN WIJK characterized GigaMethanol as so simple and so
revolutionary that the process could change the future of this
country, not just the state of Alaska. A hundred years of
natural gas reserves exist in the U.S. The U.S. can produce its
own gasoline. He said that ExxonMobil did not disagree with his
notes and he surmised that the company knows this technology is
forthcoming. He predicted the first plant would likely be built
in Texas. In response to Co-Chair Seaton, he concluded that the
first plant of this dual design would be built since Janus
Methanol AG has already built four functioning plants around the
world. He also predicted that four dual-design plants would
"kill" his current business.
3:23:06 PM
CO-CHAIR SEATON related his understanding that Mr. van Wijk's
vision is to create methanol on the North Slope, run it down
TAPS to Valdez, through a natural gas conversion plant, and ship
it to market.
MR. VAN WIJK agreed.
CO-CHAIR SEATON inquired as to whether the project would be
constructed in conjunction with the producers/owners on the
North Slope.
MR. VAN WIJK answered he has met with three of the four
producers, ExxonMobil, BP Exploration Alaska, and
ConocoPhillips. He pointed out that ExxonMobil suggested that
he travel to Alaska to discuss and convince other producers to
join. He offered his belief that he could go to the bank for
financing the moment one or two of the producers were on board,
but at this point his company needs partners. ConocoPhillips
said it would not sell the natural gas since it wants to sell
gasoline, but BP Exploration Alaska has expressed some interest
in the project. He opined that does not make sense to keep
pumping the gas back down into the well since the producers want
to earn profits and could do so with his technology. He
estimated that the proposed project would produce $1.28 million
per day for the producers and it could be up to seven times
greater than that based on natural gas alone, he said.
3:25:38 PM
CO-CHAIR SEATON indicated the legislature has been reviewing
gas-to-liquid (GTL) technology, although it has not yet looked
at Janus Methanol AG's technology. This technology appears to
be more efficient than other processes. The legislature has
been aware of the wax issues using the Fischer-Tropsch process.
He related his understanding that methanol does not seem to have
those same issues. The legislature has also been discussing
royalty and tax methods with the Department of Revenue,
including discussions on point of production and not taxing up-
front. He appreciated today's presentation as it represents one
potentially good option to consider how to monetize North
Slope's natural gas.
3:27:46 PM
SENATOR WAGONER suggested having a joint meeting in Anchorage at
a future date.
CO-CHAIR SEATON agreed that would be advisable. He indicated
the committee has two photographs that were recently donated.
CO-CHAIR FEIGE described the photographs as one of the Delta
barley fields and another of hay fields on the Kenai Peninsula
donated by the Alaska Farm Bureau.
3:29:41 PM
ADJOURNMENT
There being no further business before the committee, the House
Resources Standing Committee meeting was adjourned at 3:30 p.m.
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