Hot water system

A versatile hot water supply system incorporating a feedback control network and vapor generator of the kind in which a fuel air mixture is combusted in a chamber through which water is flowed. The vapor generator produces a low pressure steam which is permitted to mix with a low pressure water supply at a controlled rate dependent upon the desired temperature and rate of flow of the resultant mixture. The steam formed in the vapor generator is a product of fuel combustion and evaporated feed-water accompanied by the noncondensibles remaining after combustion in the vapor generator. The vapor generator may be run on transportable fuels and therefore affords portability to the system. Control systems are coupled to temperature sensors and related feedback devices and permit the efficient and advantageous use of low pressure steam and condensibles to produce high temperature water at low or high pressures. An upstream, cold water reserve provides high volume, variable temperature capacity to the system. A down-stream holding tank is also provided with the system for providing high volume, high pressure capacity at a level not normally available in locations remotely situated from conventional utility systems.

BACKGROUND OF THE INVENTION 
The present invention relates to hot water supply systems and, more 
particularly, to a versatile hot water supply system incorporating a vapor 
generator. 
Hot water systems of conventional design generally incorporate a feedwater 
boiler where large amounts of cold water are stored and heated to a 
selected temperature which depends upon demand requirements. Such 
applications include industrial hot water feed lines, schools and office 
buildings and commercial hot water markets such as car washes and 
airports. Water demand generally fluctuates in such instances and much 
energy can be lost from heating large boilers during time of inactivity. 
Commercial hot water markets may include construction sites in locations 
often not accessible to utility lines. This presents the obvious problem 
of how to heat the water. 
Various prior art embodiments have addressed the need for versatile hot 
water supply systems which meet the needs of intermediate flow demands and 
remote utilizations. Certain prior art systems have incorporated 
"in-line", electrical heating elements which directly engage the high 
pressure water flow along a select flow path for heating the water to a 
select temperature as it passes through the heater. Problems of cost, fuel 
energy conservation and limited demand capacity have been found to be 
prevalent in such systems. 
Industrial applications which are remotely disposed from power utility 
systems present a myriad of additional problems for efficient hot-water 
systems. Concrete batching plants for example, are generally used in areas 
not having hot water, much less energy supply lines. Such applications 
include concrete paving of remote areas and/or the building of concrete 
structures. Hot water boilers and/or other prior art hot water heating 
elements are of extremely limited use in such markets. While combustion 
fuel is, or may be plentiful, means for safely and efficiently utilizing 
combustible fuel to meet varying hot water supply demands is severely 
limited by prior art designs. 
One difficulty encountered in combustion fuel hot water supply units of the 
prior art is the high carbon monoxide content in the end product. This 
difficulty is particularly prevalent in prior art fuel vaporizers. Such 
noxious vapor content is objectionable around human occupation; a 
generally occurring condition where hot water is needed. High carbon 
monoxide production is traceable to incomplete combustion, in the main, 
which is in turn traceable, in part, no difficulties in maintaining stable 
flames in most prior art vaporizing units. Excessive quenching of flames 
through direct radiative and convective contact between the flame and the 
feedwater is often the cause. The advantages that vapor generators might 
have in hot water supply systems have been overlooked in light of these 
problems and in view of the low pressure steam produced. To be effective, 
low pressure steam must be automatically convertible to high pressure hot 
water upon demand. Prior art systems have not shown such capabilities and 
these hot water supply problems still exist. 
The method and apparatus of the present invention address such hot water 
supply needs and overcomes the problems of the prior art by providing a 
low pressure, vapor generator in which a demand sensitive product stream 
substantially free of carbon monoxide and other deleterious end use gases 
is produced. The vapor generator of the present invention may also be used 
in remote areas to produce a water-steam product at a sufficiently high 
heat energy state to convert large cold water supplies relatively quickly 
into hot water at either low or high pressure. 
SUMMARY OF THE INVENTION 
The present invention relates to a hot water supply system incorporating a 
low pressure vapor generator for providing either low pressure or high 
pressure hot water in a demand-sensitive configuration. More particularly, 
one aspect of the present invention relates to a hot water supply system 
utilizing combustion of fuel and air and the mixture of water, steam and 
non-combustibles to provide resultant hot water at a select temperature. 
The system comprises a vapor generator of the type having a chamber for 
the receipt and combustion of a fuel-air mixture. Means are provided for 
supplying feed water to the chamber for the conversion of feed water, fuel 
and air to steam and non-condensibles therein. Means are also provided for 
conveying the steam and non-condensibles away from the vapor generator and 
selectively delivering supply water to be heated to the steam and 
non-condensibles. At least one "zone" is provided in communication with 
the conveying and delivering means for the mixing of the water to be 
heated with the steam and non-condensibles and production of resultant hot 
water therefrom. Means are provided for sensing the temperature of the 
resultant hot water and producing an output signal in response thereto. 
Control means are provided for detecting the output of the sensing means 
and controlling the supply water delivery means for regulating the flow of 
the supply water and, correspondingly, the temperature of the resultant 
hot water. 
In another aspect, the invention includes a method and apparatus for 
producing hot water with a fuel such as natural gas or hydrogen with no 
deleterious by-products. The low pressure generator includes a three zone 
flame unit for establishing initial combustion in a reliable fashion and 
maintaining that combustion in the vaporizor unit. In the first zone a 
stoichiometric mixture is ignited and burned under shielded conditions 
which ensures flame stability. In the second zone excess air is introduced 
to the flame under shielded conditions to insure completion of combustion; 
and in the third zone, the flame is exposed to the feed water to vaporize 
it and quench the flame after combustion has been completed. Such a unit 
may then provide low pressure clean hot steam and non-condensibles usable 
around human occupancy. A temperature sensor samples the quality of the 
steam produced from the vapor generator. When steam of a sufficient 
quality is produced a control unit sensing the steam condition actuates a 
flow valve from a high volume cold water supply and allows the cold water 
to integrate with the high temperature steam. A downstream temperature 
sensor then relays the temperature of the steam-water mixture. This 
information is inputted into the control unit to govern the amount of 
water permitted to mix with the low pressure steam. When the desired 
temperature of the product mixture is achieved for that particular state 
of operation, the water mixture may be tapped for immediate use or 
directed into a water storage tank. 
In accordance with another aspect of the invention, an improved vapor 
generator is provided in conjunction with a water storage unit having 
temperature and high and low water level sensing units. Data from the 
sensing units is inputted into the control unit to activate the cold water 
supply reservoir for mixture with the output of the vapor generator. The 
storage tank water may then be used at high or low pressure by the 
incorporation of an additional pumping unit. In addition, the temperature 
of the holding tank water may be controlled by the addition of high heat, 
steam-water flow from the generator. This aspect of the invention 
facilitates high heat storage with no high pressure considerations. 
Moreover, chemical additives may be incorporated in the storage tank 
pumping unit at various stages and/or temperatures for select applications 
in industry, commercial hot water markets and/or oil well pumping systems.

DETAILED DESCRIPTION 
Referring first to FIG. 1, there is shown a diagrammatic view of one 
embodiment of a method and apparatus for hot water production construction 
in accordance with the principles of the present invention. A hot water 
supply system 10, diagrammatically shown, includes a low pressure vapor 
generator 12, a programmable temperature-flow control unit 14, water 
supply means, associated flow conduit, and sensor and flow control means. 
The control unit 14 is coupled to upstream and downstream temperature 
sensors 16 and 18, respectively, which relay data to a temperature monitor 
20. The monitor 20 is linked to the control unit 14 for 
temperature-sensing and responsive actuation within system 10. Control 
unit 14 is programmed to responsively actuate generator 12 and the flow 
valves governing the inflow and mixture of the generator fluid product 75 
and cold supply water into conduit or flow channel 15 at the necessary 
rates to produce a heated fluid body 99 at a selected temperature and 
flow. In this manner, specific hot water demands of time, temperature, 
volume and pressure, can be efficiently met on an immediate use or long 
term storage basis. More over, the demands for the desired hot water can 
be met at high or low pressures, with or without chemical additives, and 
with apparatus lending itself to set-up and use in remote areas where 
utility services may not be available. 
Addressing first the low pressure generator of the present invention, there 
is shown a vaporizer unit designated generally as 12. It may include a 
vapor generator of the type shown and described in my U.S. Pat. No. 
4,211,071 assigned to the assignee of the present invention. The primary 
component thereof is the vaporizer proper or main combustion chamber 13. 
Chamber 13 is preferably an upright closed-ended elongated cylinder 
adapted to enclose the bulk of the flame generated in accordance with the 
invention. To the bottom of chamber 13 is connected a product exit line or 
conduit 15. Chamber 13 has a cylindrical outer wall 17, and closed ends 
19, 21. Provision is made for the delivery of feed water to the interior 
of the main combustion chamber. The provisions include inlet water line 
23, and internal cylindrical wall or tube 25. Tube 25 is attached to 
bottom end of 21 and terminates a selected relatively small distance short 
of top end 19. An annular space 27 is thus established between walls 17 
and 25 extending over substantially the full height of chamber 13. 
In operation of the generator 12 of this particular embodiment, feed water 
is delivered into annular space 27 through inlet line 23. The water cools 
the unit and is warmed as it rises through the annular space or jacket 27. 
The water then spills over the top edge of tube 25, and flows down its 
inner wall. During the first part of the downward travel, the water 
absorbs heat conductively from a shielded portion of the flame. During the 
final part of its downward flow, the feed water is in direct radiative and 
convective contact with part of the flame, and is vaporized thereby to 
form steam that becomes part of the product stream leaving chamber 13 via 
conduit 15. 
The fuel and air delivery system of the invention is designated generally 
as 40. It includes an air compressor 41, having an air filter (not shown). 
Various types of compressors having suitable output pressures and delivery 
rates may be employed. The compressed air issuing from compressor 41 
enters conduit 43. 
The compressed air stream in conduit 43 is divided into two streams bearing 
a selected ratio (volumetric or mass) to each other. The division is 
accomplished by providing mixing conduit 44, which is an extension of air 
conduit 43, and branch or auxiliary air conduit 45. Conduits 44 and 45 are 
each connected to the precombustion chamber 50. Air flow dividing orifice 
plates 46 and 47 are mounted in conduits 44 and 45 adjacent the branching 
or division point, and the orifices in the plates are sized to bring about 
the desired division of the air flow. Preferably, the volume of flow 
through auxiliary air conduit 45 amounts to about 8 to 10 percent of the 
air flow through mixing conduit 44. 
Immediately downstream of orifice plate 46 in mixing conduit 44 there is 
provided a fuel inlet 48. Flow in conduit 44 just downstream of the 
orifice plate 46 is quite turbulent, and it is desirable to introduce the 
fuel at this point to initiate thorough and intimate mixing of the fuel 
and air. Furthermore, it is preferred that mixing conduit 44 be fairly 
long in order to provide a full opportunity for thorough mixing of the air 
and fuel stream before it reaches the precombustion chamber. Mixing is 
also enhanced by the directional change in conduit 44 at bend or elbow 49. 
The diameter of mixing conduit 44 is selected in view of the desired flow 
rate so that the lineal velocity of the mixture flowing therethrough is 
substantially equal to or slightly greater than the flame propagation 
speed, so that the flame established and maintained in the precombustion 
chamber cannot migrate back up into conduit 44 or its bend 49. For 
example, with a designed fuel flow of 17 cubic feet per minute, mixed with 
a stoichiometric quantity of air, a nominal conduit diameter of about 2 
inches is satisfactory. 
The precombustion chamber of the vapor generator of the present invention 
is designated generally as 50. It includes a cylindrical housing 51, 
somewhat larger in diameter than opening 52 in the upper end 19 of chamber 
13. The upper end of housing 51 is closed by plate 54. A flame enclosing 
skirt or shield 59 depends downwardly from plate 54, terminating short of 
opening 52 so that a circular slot 55 is defined between the outer edge of 
the skirt and the inner edge of the flange. A cylindrical annular space 56 
is defined between skirt 59 and housing 51. Conduit 44 is attached to the 
top of the precombustion chamber to deliver a fuel-air mixture into the 
space within shield 59. Conduit 45 is attached to the side of the 
precombustion chamber to deliver auxiliary air into the annular space 56. 
A pilot burner assembly, (not shown), is mounted on precombustion chamber 
50 so that its mouth opens preferably into the chamber near the junction 
of conduit 44 and plate 54, and within skirt 59. In the vaporizer 13, a 
second flame enclosing shield or skirt 58 is mounted to top end 19 to 
depend downwardly from opening 52. The pilot flame thus formed in the 
pilot burner issues into the precombustion chamber to initiate combustion. 
As can be seen from the foregoing, three primary input streams are involved 
in the generator 12: fuel gas; combustion supporting gas (preferably air 
from an electrically driven blower or compressor); and water. There are 
thus three primary points of control which are coordinated by control unit 
14: fuel, air and water. Fuel metering valve 61 and feed water flow valve 
62 are provided, each remotely actuatable by control unit 14. During 
start-up, fuel gas and sparking current are supplied to the pilot burner. 
During operation, a series of monitoring devices monitor various operating 
conditions and turn the generator 12 off, or prevent its start-up if it is 
already off, when a condition departs from a desired value or range of 
values. These monitors include thermostats, water level sensors and fuel 
pressure switches which provide generator operations with low level carbon 
monoixide production. 
The particular embodiment of the present invention shown herein comprises 
the improved generator 12 working with a cold water supply which may 
simply be a water utility line 24a or a supply system 22 for providing the 
requisite water to be heated. The system 22 may be coupled to a passive 
body of water such as a lake (not shown) or a water utility line 24a. In 
the event supply water is taken directly from a pressurized utility line 
24a, system 22 would be by-passed as shown in phantom by line 24b. The 
system 22 preferably comprises a storage reservoir 24, water supply line 
24a and pumping network 26. A pump 28 is provided for high pressure 
circulation of water through conduit 30 out of the reservoir 24. The size 
of reservoir 24 may vary depending on maximum supply demands. A relief 
valve 32 may permit the flow of water back to the reservoir 24 in 
situations where pressure must be released. A remotely actuatable flow 
valve 34 governs the volume of flow of water from the pumping network 26 
to vapor generator discharge flow line 15. A second on-off valve 36, 
remotely actuatable from control unit 14 may also be provided for quickly 
stopping or starting the flow of water between reservoir 24 and conduit 
15. 
Supply water to be heated enters the channel or flow pipe 15 through cold 
water supply duct 64. The unheated, or cold, supply water initially 
contacts the generator product 75, comprising evaporated feedwater, water 
vapor of combustion, and non-condensibles produced by the generator 12, in 
open flow communication within pipe 15. A mixing chamber 65 (shown 
partially in phantom) is provided downstream of supply duct 64 to 
facilitate thorough mixing and heat transfer of these normally active 
constituents. The chamber 65 is shown in phantom because it could, in 
various configurations, comprise a valve, an orifice or simply a 
downstream section of flow pipe 15. The particular design of chamber 65 
depends upon various design aspects of system 10 such as volume, pressure 
and temperature differentials between supply water and the fluid product 
75. 
The operation of the present invention can be seen to require specific 
control of the mixture of supply water and the fluid product 75 of 
generator 12. Cold water may be seen to come from a variety of sources 
such as conventional utility line 24a. Of course, this connection 
substantially restricts the system 10 to the capacity of utility line 24a. 
In remote locations where volumes of hot water of select temperatures are 
not beyond the capacity of available water utility lines, such 
configurational simplifications are feasible and within the scope of the 
present invention. The term capacity, however, refers both to the pressure 
and volume at which such utility lines can deliver water to supply duct 
64. 
The present invention is particularly adapated for applications where 
utility lines are not available and high volume, hot water is needed. The 
supply system 22 provides such versatility. A storage reservoir 24 
comprising a conventional storage tank or tanks, provides the capacity of 
high volume water feed into duct 64 during periods of demand beyond the 
capacity of available water systems. For example, underdeveloped and/or 
disaster areas often experience low water pressure and limited supply 
capacity. Tornados and hurricanes often cause such problems. In those 
instances, the storage reservoir 24 of the present invention is connected 
to supply pump 28, which feeds water through pipe 30, valves 34 and 36 to 
duct 64. The reservoir 24 can be of any size and can be supplied and/or 
pressurized by conventional supply line 24a or by an alternate pump 
system. Pump system 24c is shown in phantom to illustrate an available 
option for pumping water from alternate supplies such as lakes and/or 
temporary storage facilities (not shown). It may thus be seen that a wide 
range of options exists for supply water whether the system 10 is used 
with utilities or situated in remote, disaster or underdeveloped areas. 
Once sufficient fuel and supply water is made available, as described 
above, the system of the present invention can produce hot water of 
selectable temperature and volume and do so within a wide range of time 
frames. The control of these production parameters is made possible by 
coordination of generator 12 operation, fluid temperatures and regulated 
flow rates from the control unit 14. As shown in FIG. 1, the volume of 
water from duct 64 may be controlled by valves 34 and 36, actuatable by 
control unit 14. The valves 32, 34, 36 and 66 may be of the conventional 
solenoid actuated variety. To coordinate such efforts, the control unit 14 
preferably includes a conventional programmable computer capable of being 
programmed with the desired temperature, volume and time frame in which 
the final product is needed. The system 10 start up is thus the first 
phase of operation. The unit 14 also coordinates a second phase of 
continued operation and therein must sense variable input data, analyze 
the data relative to the production parameters and make responsive changes 
to the various control areas of the system 10. 
In Phase I operation, the desired temperature, volume and demand time for 
hot water are programmed into the control unit 14 as production 
parameters. Ambient temperature sensors 16a and 16b communicate to the 
control unit 14 the initial working temperatures of the feed water and the 
supply water to be heated, respectively. This data forms a basis for a 
determination of a projected mixture ratio of heated feed water and cold 
supply water. The data of desired discharge volume is then determinative 
of the projected flow rates of the respective constituents. The control 
unit 14, having received the above data and determinative operational 
parameters, then activates one of a series of preprogrammed start-up 
sequences of the generator 12 to cause it to operate at the most optimal 
fuel-air-water ratio for the particular parameters involved. 
It may thus be seen that the control unit 14 preferably includes a 
plurality of preprogrammed, Phase I start-up sequences for the various 
catagories of production parameters. These sequences are designed for 
maximizing operational efficiency through the Phase I start-up at 
particular demand levels. For example, if 1000 gallons (V.sub.1) of water 
at 100. F. (T1) were needed over a 3 hour time frame, (A.sub.1) the 
generator 12 could be run at a much lower combustion level (L.sub.1) than 
the same remaining production parameters needed over a 1 hour time period 
conserving fuel and maximizing the efficiency of operation. The controlled 
combustion level (L.sub.2) could likewise be maintained at the (L.sub.1) 
level even if the temperature (T.sub.2) were raised to 180. F., if the 
demand time frame (A.sub.2) was expanded sufficiently. A combustion level 
(L.sub.3) if a substantially higher volume (V.sub.3) of heated water was 
needed. The algorithm for solving such operational requirements is 
determined by conventional mathematical, programming methods and fed into 
control unit 14. 
Once the system 10 passes through the Phase I start-up and becomes operable 
at the flow rates and settings which were projected by control unit 14 to 
be optimal for a particular demand, the actual fluid temperatures become 
controlling which constitutes the second phase of operation. The vapor 
generator 12 needs a predefined period to reach a stabilized output. 
Following this stabilization period, a Phase II program in control unit 14 
takes over. This program is likewise determinable by conventional 
mathematical programming techniques and includes receiving temperature 
data from sensors 16 and 18 and analyzing it. 
Sensor 16 detects the temperature of the upstream fluid product of 
generator 12, described above. The heat content of this high temperature 
fluid, referred to as fluid product 75 comprising evaporated feed water 
and non-condensibles, is readily calculable and the monitor 20 stores and 
relays this information to control unit 14 for comparison with the 
downstream temperature condition of sensor 18. It should be noted that 
such segregation of function between monitor 20 and control unit 14 is 
presented for purposes of clarity. The heat content of the fluid product 
75 engaging the heat sensor 16 is readily calculable from the volume of 
input feed water from channel 23 and the volume of fuel and air from valve 
61 and pump 41, respectively. Once these factors are fed into the control 
unit 14, the heat content (Q.sub.1) of the fluid product 75 detected by 
temperature sensor 16 is determinable. The actual heat content Q.sub.2 is 
compared to the programmed Q.sub.1 and adjustments in the three primary 
points of control of the generator 12 are effected by unit 14. 
The heat content of the fluid 75 may also be used to vary the volume of 
flow, of "cold", unheated supply water from cold water duct 64. The 
temperature of this supply water does not have to be known although sensor 
16b is so shown as a source of usable input data. Temperature sensor 18 
alone can be used to measure downstream temperature and relay information 
to monitor 20 and to control unit 14. If the temperature is too low, 
either higher heat content from the generator 12 is needed or less "cold" 
water. This decision is implemented through control unit 14 which is 
programmed to adjust the respective flow rates toward the optimal 
efficiency levels discussed for Phase I operation. In this manner the 
system 10 is not limited in operational scope by any one factor. Both 
"cold" water supply volume and vapor generator heat output may be adjusted 
according to changes in operation conditions. Each can be automatically 
programmed in the present invention to balance parameter variation 
deficiencies in the other to produce a heated fluid body 99, discharging 
at the most optimal rate for a desired temperature, volume and pressure. 
The output rate of the discharging fluid body 99 produced in system 10 may 
be seen to be directly regulated by flow valve 66 in conjunction with the 
aforesaid operational parameters. An input data terminal 80 is 
illustratively shown in FIG. 1 and allows above described programming of 
control unit 14. The optimal temperature, volume, pressure and rate of 
flow for the resultant fluid body 99 discharged from chamber 65 is thus 
regulated by the control unit 14 in conjunction with the scheduled 
programming and actual parameters encountered. The fluid body 99 within 
the chamber 65 generally comprises low pressure, heated supply water, 
evaporated feed water and the non condensibles produced by the generator 
12. In certain applications, this active fluid mixture may be directly 
usable. Such use depends upon the "upstream capacity" which refers to the 
operation level of the generator 12 and volume of supply water available. 
For example, with sufficient upstream capacity, the fluid body 99 from 
chamber 65 may be channeled through an "end" use conduit 82 directly to 
fluid pumping unit 83 for generating desired high pressure discharge. 
Conduit 82 and pump 83 comprise one use configuration shown in phantom for 
purposes of clarity. Also shown in phantom is another use configuration 
embodied in a simple discharge outlet 84 for conventional collection of 
the subject fluid 99. 
Referring now to FIG. 1A, there is shown a concrete mixing truck of 
conventional design wherein heated water may be used to mix cement. It may 
be seen that such an application requires little water pressure and use 
may be intermittent in nature. For this reason, the present invention is 
particularly useful in heating water to mix concrete and provides an 
unlimited operation capacity for remote areas where concrete construction 
is often the initial vestage of civilization. Such a hot water supply is 
also useful as a means of heating and personnel use in remote areas. 
High pressure hot water is a marketable commodity in itself and has a 
variety of commercial uses. One such market is presented in FIG. 1, in the 
diagrammatical form of car wash system 90. A car 92 is shown positioned in 
a stall 94 with a hot water discharge head 96 atop the car. The water 
sprayed from the head 96 is generally hot, under pressure and selectively 
mixed with soap or wax. Car wash operations inherently require high 
volumes of high pressure hot water but on an intermittent demand scale. 
For example, during rainy weather demand can be zero, but within an hour 
of clear skies, demand can exceed conventional capacity. 
The present invention provides the capacity of a high volume, high pressure 
hot water discharge through the incorporation of a downstream storage tank 
100. This particular embodiment permits the relatively low pressure, fluid 
discharge from chamber 65 to be collected for use in a myriad of high or 
low pressure applications. The storage tank 100 includes an output pumping 
network 102 and input settling system 104. The pumping network 102 
comprises a discharge pipe 106 in combination with a regulating valve 108. 
Downstream of the regulating valve, an optimal, fluid intake line 110 is 
provided for drawing either chemical additives or water from a second 
water supply (not shown). A pump 112 then creates the requisite discharge 
pressure and channels the discharge water through conduit 114 to its end 
use. In this particular embodiment, the end use is shown as the car wash 
90 discussed above. The election between the use of conduit 82 and tank 
100 may be determined simply by demand. If maximum use demand can be 
supplied by the direct fluid output from chamber 65 it is possible to 
pressurize the fluid by pump 83 directly. The inherently active mixture of 
heated supply water, evaporated feed water and non condensibles produced 
by the generator 12 then forms an ideal mixture for car wash applications. 
Moreover, the combination is usually of such an active nature it 
necessitates the "settling tank" features of tank 100 set forth herein. 
Referring particularly now to the right hand portion of FIG. 1 comprising 
the tank 100, hot water 150 may be maintained at a level 152 beneath an 
output port 154 in the side wall 156 of the tank. The port 154 is in 
direct flow communication with mixing chamber 65 and may serve as a 
discharge port for said chamber or may be spaced therefrom by a section of 
conduit 158. The configuration of tank 100 is perferably such that the 
port 154 discharges the active fluid body 99 in a tangential fashion. A 
tangential entry creates a vortexual swirl of the heated supply 
water-evaporated feed water mixture. In the vortexual swirl, the non 
condensibles are allowed to separate out from the mixture to leave usable 
hot water 150. The non condensibles and unmixed steam of the discharging 
fluid body 99 rise upwardly within the tank 100. A demisting screen 160 is 
provided to collect and condense rising steam and return it to the 
settled, hot water 150 therebelow. A vent 162 then permits escape of the 
non condensibles. 
In operation, the tank 100 is coupled to a water level sensor package 170 
comprising an upper and lower level detector 172 and 174, respectively, 
Water level signals from detectors 172 and 174 are received by tank 
monitor 176 which communicates with control unit 14 for coordination of 
the production of fluid body 99. Temperature sensor 178 may be provided in 
tank 100 to monitor the temperature of the stored water 150. This 
temperature may be received and relayed by tank monitor 176 to control 
unit 14. In this manner discharge fluid 99 with an increased heat content 
can be provided to heat the stored water 150 as necessary to maintain its 
usefulness over prolonged storage periods. 
It is thus believed that the operation and construction of the present 
invention will be apparent from the foregoing description. While the 
method and apparatus shown and described has been characterized as being 
preferred it will be obvious that various changes and modifications may be 
made therein without departing from the spirit and scope of the invention 
as defined in the following claims.