Donald ERICKSON
ISAAC Solar Icemaker
ISAAC Solar Ice Maker
The ISAAC Solar Icemaker is
an Intermittent Solar Ammonia-water Absorption Cycle. The ISAAC
uses a parabolic trough solar collector and a compact and
efficient design to produce ice with no fuel or electric input,
and with no moving parts.
The ISAAC Solar Icemaker operates in two modes. During the day,
solar energy is used to generate liquid ammonia refrigerant.
During the night, the generator is cooled by a thermosyphon and
ice is formed in the evaporator compartment as ammonia is
reabsorbed to the generator.
The daily ice production of the ISAAC is about 5 kg per square
meter of collector, per sunny day. The construction of the ISAAC
Solar Icemaker involves only welding, piping and sheet metal
work, and there are no expensive materials. It is estimated
that, when produced in-country where wages are low and
transportation costs can be minimized, the 11 square meter
ISAAC can be produced for less than $7,000. When produced
in-country, the creation of urban employment is an additional
advantage of ISAAC technology.
The characteristics of the ISAAC which make it particularly well
suited to provide refrigeration to unelectrified rural
communities are:
1. It is solar thermally powered, avoiding expensive diesel fuel
or photovoltaics.
2. Low cost construction requires only welding, piping and sheet
metal work.
3. Very low maintenance.
4. The quantity of ice is sufficient to support small scale
businesses while maintaining sustainability in fragile
environments, or provide low cost household refrigeration.
The ISAAC design was developed by Energy Concepts Company. Over
forty systems have been built and twenty installed in seven
countries. The ISAAC is on display in Annapolis, Maryland and at
Sandia National Lab, Albuquerque, New Mexico. ISAAC is now being
distributed and commercialized by Solar Ice Co.
Providing Jobs to Remote
Communities - By Providing Ice
The ISAAC Solar Icemaker makes enough ice at low cost to support
many small scale businesses in rural unelectrified areas.
Enterprises using ISAAC will be environmentally sustainable
because no fuel is required. They will be economically
sustainable because the cost of producing the ice by the ISAAC
is sufficiently less than the value of the ice that it can
easily be recovered by a micro-enterprise.
Ice is of major economic importance. In rural communities of
developing countries, there is frequently a shortage of ice to
support business activities. The result is loss of revenue,
jobs, and substantial food spoilage.
Three important community needs for electricity are:
* lights
* communications and entertainment
* refrigeration.
Lights, communication and entertainment require modest amounts
of electricity and are affordable even at the high cost of
electricity from emergency generators, diesel mini-grids or
photovoltaics.
When refrigeration is needed also, the amount of electricity
required from the power system increases drastically. Thus it is
usually omitted to keep costs down. An ISAAC Solar Icemaker
supplies refrigeration without the intermediary step of
electricity and at a much lower cost. Thus ISAAC Solar
Icemakers, in combination with mini-grids and/or photovoltaics,
are a good method of supplying remote community needs.
For example, ISAAC can provide domestic refrigeration. An ISAAC
produces six blocks of ice each day, weighing ten kilograms
each. If an icebox requires five kilograms of ice per day to
stay cool, then one ISAAC will be able to supply domestic
refrigeration to twelve households. The cost of a standard
electric refrigerator, plus the constant requirement of
expensive electricity, would be much higher.
The
Absorption Cycle was invented in 1846 by Ferdinand Carré for
the purpose of producing ice with heat input. It is based on
the principle that absorbing ammonia in water causes the vapor
pressure to decrease. Absorption cycles produce cooling and/or
heating with thermal input and minimal electric input, by
using heat and mass exchangers, pumps and valves.
An
absorption cycle can be viewed as a mechanical
vapor-compression cycle, with the compressor replaced by a
generator, absorber and liquid pump. The absorption cycle
enjoys the benefits of requiring a fraction of the electrical
input, plus uses the natural substances ammonia and water,
instead of ozone depleting halocarbons. The absorption cycle
enjoyed widespread use from the 1920’s as gas powered
refrigerators/ice-makers.
The
basic operation of an ammonia-water absorption cycle is as
follows. Heat is applied to the generator, which contains a
solution of ammonia water, rich in ammonia. The heat causes
high pressure ammonia vapor to desorb the solution. Heat can
either be from combustion of a fuel such as clean-burning
natural gas, or waste heat from engine exhaust, other
industrial processes, solar heat, or any other heat source.
The high pressure ammonia vapor flows to a condenser,
typically cooled by outdoor air. The ammonia vapor condenses
into a high pressure liquid, releasing heat which can be used
for product heat, such as space heating.
The
high pressure ammonia liquid goes through a restriction, to
the low pressure side of the cycle. This liquid, at low
pressures, boils or evaporates in the evaporator. This
provides the cooling or refrigeration product. The low
pressure vapor flows to the absorber, which contains a
water-rich solution obtained from the generator. This solution
absorbs the ammonia while releasing the heat of absorption.
This heat can be used as product heat, or for internal heat
recovery in other parts of the cycle, thus unloading the
burner and increasing cycle efficiency. The solution in the
absorber, now once again rich in ammonia, is pumped to the
generator, where it is ready to repeat the cycle.
An
absorption cycle can use a variety of working pairs. The
working pair is made up of a refrigerant, typically ammonia or
water; and a solution which absorbs the refrigerant. Other
working pairs include lithium-bromide-water; TriDroxide-water;
and Alkitrate-water. Tridroxide and Alkitrate are Energy
Concepts patented working pairs with specialty applications in
industry.
Absorption
cycles can operate at high efficiency by utilizing advanced
cycles, using generator-absorber heat exchange, multiple
pressures, and multiple effects. These cycles use extensive
internal heat recovery to require less prime fuel input to
produce the same thermal output. High efficiency operation,
plus benefits of environmentally friendly refrigerants,
clean-burning fuels, and few moving parts requiring
maintenance make absorption a very good choice for consumers.
Absorption cycles can
produce a variety of thermal outputs. In common commercial use
today are gas-fired absorption chillers, which produce chilled
water for space cooling applications. The absorption cycle can
produce low temperature cooling for ice production or cold
storage. Turbine inlet cooling is a very efficient use of
absorption cooling, boosting turbine efficiency by up to 15%.
Many other applications exist in industry, where waste heat is
available and cooling is required. Advanced cycles can also
produce electrical or shaft power by producing steam or high
pressure vapor to power a turbine/generator pair.


Publications -- ISAAC™
SOLAR
ICEMAKER
Pierpont, J. P. "Energy Concepts Rises From Ashes To
International Market." Baltimore Business Journal.
February 1989.
"What’s New: News in Brief." Maryland Business Weekly: The
Baltimore Sun. December 18, 1989.
"Hot Refrigeration" Environmental Protection Week. June
1990.
"Solar Refrigeration Brings Ice to Developing Countries." Solar
Industry
Journal. Second Quarter. 1990.
Maier, Timothy A. "Solar-Powered Refrigerator Heats Up Energy
Concepts." Baltimore Business Journal. November
1990.
Erickson, Donald C. "Isaac Solar Absorption Icemaker." Soltech
91
Erickson, Donald C. "Isaac Solar Refrigerator." Environment-Friendly
Technologies
for the 21st Century. Proceedings of the Japanese Assocition
of Refrigeration Absorption Heat Pump Conference. Tokyo.
September 1991.
Erickson, Donald C. and Jorgensen, Paul. "Solar Absorption
Ice-Making in a Mexican Fishing Village." Hawaii 1992.
Erickson, Donald C. "Solar Icemakers in Maruata, Mexico." Solar
Today. July/August 1994.
ThermoSorber™
The ThermoSorber™ is a gas-fired heat pump which
supplies air conditioning or refrigeration at the cold end,
and which uses all the reject heat (gas heat plus cooling duty
) to heat hot water. The high temperature glide achieved with
the GAX absorption cycle makes it possible to heat hot water
to 160°F, thus meeting the needs of commercial users. The hot
water is normally the primary product, with the cooling in a
supplementary role. This ensures high year round utilization
and short paybacks. This appliance reduces the utility bill
for hot water and cooling by more than half, compared to the
most economic commercially available equipment.
US6584801
Absorption Cycle with Integrated
Heating System
Abstract -- An absorption
system powered by low temperature heat for producing at least
one of refrigeration and power is disclosed, wherein a
low-pressure drop heat reclaimer 1 reclaims heat from the source
into a heating agent, which in turn supplies heat to the
absorption cycle desorber 5 via internal coils 7. The extra
temperature differential normally present in closed cycle
heating systems is avoided by using the absorption working fluid
as the heating agent, in an integrated system.
US6269644
Absorption Power Cycle with Two
Pumped Absorbers
Abstract -- An absorption
power cycle is disclosed which achieves a closer match to heat
source temperature glide, and also lower heat source exit
temperatures, and hence higher conversion efficiencies, in
practical equipment. Referring to FIG. 7, two separate absorbers
(725 and 706) are provided, each with a pumping path for a
different concentration absorbent liquid to a different
temperature location within counter-current high-pressure
desorber 721. Heat source 710 heats the high-pressure desorber
721 and superheater 724 in parallel, and subsequently heats
intermediate-pressure desorber 761. Dotted lines in the figures
signify vapor.
US5309985
Stationary Continuous
Multimodular Trisorption Heat Pump
Abstract -- Apparatus and
process are disclosed for sorption heat pumping at high
efficiency in a smooth and continuous manner using a
multiplicity of stationary triplex sorption modules. The
hermetically sealed trisorption modules, each of which contains
at least two solid sorbents, are free of pumps, valves,
restrictors, or any similar devices for flow control of
refrigerant or sorbent. The apparatus contains no moving parts
beyond a small number of control and motive devices for the heat
transfer fluids. The preferred refrigerant is ammonia and the
preferred sorbents are the solid type with monovariant
equilibrium, e.g., BaCl2, SrCl2, CaCl2, MnCl2, FeCl2 and SrBr2.
The apparatus is preferably adapted for residential or
small-scale commercial space-conditioning applications, and
operates at double-effect efficiency in both the heating and
cooling modes without inter-module heat transfer.
US5279359
Rotary Trisorption Heat Pump
Abstract -- Apparatus and
process are disclosed for sorption heat pumping at high
efficiency in a smooth and continuous manner using a
multiplicity of intermittent cycle triplex sorption modules. The
hermetically sealed trisorption modules, each of which contains
at least two solid sorbents, are free of pumps, valves,
restrictors, or any similar devices for flow control of
refrigerant or sorbent. The preferred refrigerant is ammonia and
the preferred sorbents are the solid type with monovariant
equilibrium, e.g., BaCl2, SrCl2, CaCl2, MnCl2, FeCl2 and SrBr2.
The apparatus is preferably adapted for residential or
small-scale commercial space-conditioning applications, and
operates at double-effect efficiency in both the heating and
cooling modes without inter-module heat transfer.
US5272891
Intermittent Sorption Cycle
with Integral Thermosyphon
Abstract -- Intermittent
sorption cycles with fixed heat supply and removal and comprised
of a generator/absorber (4), a condenser (2), and a
receiver/evaporator (10) are adapted and simplified so as to
require at most only two control valves (8) and (15) for their
operation. With an integral thermosyphon (6) for absorption heat
removal, only a single refrigerant charge is necessary. The two
valves are advantageously combined into a single three-way ball
valve, and key gravity drains (14) and (17) are provided.
Applications include hot water heating, solar refrigeration, and
steam generation.
US5653116
Triple-Effect Absorption Cycle
with Condensate-to-Solution Sensible Heat Exchanger
Abstract -- A triple-effect
cycle is disclosed which avoids the two primary limitations of
currently known triple-effect cycles: super-atmospheric
pressures and/or low pressure absorbers that operate without
mass transfer enhancers. The cycle is comprised of two hermetic
loops-one a conventional LiBr double-effect loop, and the other
a single-effect loop which overlaps the high pressure portion of
the double-effect loop, and exchanges heat with it at three
locations. Referring to FIG. 3, the latent heat exchanges are
with absorber 302, condenser 304, and evaporator 305 of the
single-effect loop. Sensible heat losses are reduced by
incorporating inter-loop condensate-to-solution sensible heat
exchanger 314. The inter-loop CSSHX also applies to other
triple-effect cycles.
US5771710
Thermosyphon Cooled Absorber for
Air Cooled Absorption Cycles
Abstract -- The absorption
step of a continuous absorption cycle apparatus (refrigerator or
heat pump) is externally cooled by an air-cooled thermosyphon
having hot end 107 (FIG. 1), air-cooled end 115, and reservoir
123. The absorption step is further recuperatively cooled by
internal fluids, in absorber heat exchanger 108 and/or GAX 109.
Thus the absorber is highly compact and the cycle is highly
efficient. A hotter hermetic thermosyphon can advantageously
supply additional cooling.
US5660049
Sorber with Multiple Cocurrent
Pressure Equalized Upflows
Abstract -- A sorber for
sorbing a vapor into (absorber) or out of (desorber) a liquid
sorbent comprised of a sequential plurality of highly effective
and intensified locally cocurrent sorptions, but with
non-cocurrent flow of vapor and liquid between the individual
sorptions. The structure containing the locally cocurrent upflow
is preferably comprised of enhanced heat transfer surface,
making the sorption diabatic, further enhancing the
intensification, and improving the sorption efficiency.
Referring to FIG. 12 , vertical cylinders (70) and (71) form an
annular space within which desorption occurs, powered by
external heat source (72) and internal heat recuperation (77).
The liquid portion of the annulus is divided into multiple
compartments by folded rectangular fin (73). The space above fin
(73) allows pressure equalization of all compartments. Each
compartment is divided by insert (80) into separate vapor-liquid
riser channels and a liquid downcomer channel. The sorbent
liquid flow sequentially through the compartments via flow ports
(74). The same high effectiveness sequential liquid
recirculating cocurrent upflow desorption can also be
accomplished in a horizontal cylindrical annulus, in plate fin
exchangers, and in other geometries.
US5713216
Coiled Tubular Diabatic
Vapor-Liquid Contactor
Abstract -- A non-diabatic
vapor-liquid contact device is disclosed which achieves high
heat transfer effectiveness without sacrificing mass transfer
effectiveness. Referring to FIG. 2, a helical coil of crested
tubing 84 is contained within the annualr space between shrouds
82 and 83. Liquid flows downward through the annulus, and vapor
flows countercurrently upward. The mass exchanging fluids pass
through the space between tube crests and the shroud, achieving
very effective mixing. Heat transfer fluid is flowed through the
tubing via connections 87 and 88. The heat and mass transfer is
preferably additionally enhanced by interspersing contact media
with the coiled tubing, either longitudinally or radially.
US5798086
Intensified Locally Cocurrent
Tray Contactors
Inventor(s): ERICKSON
DONALD C [US]
Abstract
-- An intensified means of multicomponent fluid multistage
vapor-liquid contact is disclosed. The contactor achieves the
thermodynamic advantages of global countercurrency, the tray
efficiency advantages of tray crosscurrency, and the point
efficiency advantages of local cocurrency with liquid
recirculation. Referring to FIG. 6, each tray has multiple
compartments formed by compartment dividers 62, 63, and 64, and
each compartment has a channel divider 69, 66, 67 which forms
separate locally cocurrent riser channels and liquid downcomer
channels.