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Patent 2120526 Summary

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(12) Patent Application: (11) CA 2120526
(54) English Title: PLANT FOR RECUPERATING HEAT FROM WASTE WATER
(54) French Title: INSTALLATION DESTINEE A RECUPERER LA CHALEUR D'EAU RESIDUAIRE
Status: Dead
Bibliographic Data
(51) International Patent Classification (IPC):
  • F24J 3/00 (2006.01)
  • F24D 17/00 (2006.01)
(72) Inventors :
  • BARTL, EGMONT (Austria)
(73) Owners :
  • BARTL, EGMONT (Austria)
(71) Applicants :
(74) Agent: GOWLING LAFLEUR HENDERSON LLP
(74) Associate agent:
(45) Issued:
(86) PCT Filing Date: 1992-10-02
(87) Open to Public Inspection: 1993-04-15
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): Yes
(86) PCT Filing Number: PCT/AT1992/000125
(87) International Publication Number: WO1993/007424
(85) National Entry: 1994-03-31

(30) Application Priority Data:
Application No. Country/Territory Date
A 1984/91 Austria 1991-10-04

Abstracts

English Abstract

2120526 9307424 PCTABS00021
The invention concerns a plant for recuperating heat from
preferably discontinuously arising waste water from, in particular,
domestic households, commercial and industrial premises, etc. The
plant comprises at least one counter current-flow heat exchanger
through which the waste water flows and which is connected in
circuit with at least one hot-water tank or boiler. The invention calls
for a sensor (6), designed to detect the arrival of waste water,
to be fitted in the line (10) carrying the waste water, the
sensor being connected to at least one pump (1) or to a control unit
(8) which controls the pump(s). When the sensor generates a
signal indicating the arrival of waste water, the pump (1) is switched
on and sucks the waste water in the line (10) out of the line
and through the heat exchanger (3).


Claims

Note: Claims are shown in the official language in which they were submitted.


PCT/AT92/00125
-14-

P a t e n t C 1 a i m s :
1. System for recovering heat from preferably
discontinuously arising waste water from, particularly,
households, houses, businesses, etc, comprising at least one
heat exchanger (3) through which the waste water flows,
which operates in counterflow and which is connected in the
circulation cycle of at least one warm water reservoir or
water heater (17), whereby a sensor (6) is provided in the
discharge line (10') conducting the waste water which
responds to the arrival of waste water and which is
connected to at least one pump (1) or to a control device
(8) controlling the pump(s) (1), with which pump the waste
water detected in the waste water line (10') is removed or
drawn off in the case of a signal from the sensor which
indicates the arrival of waste water and conducted or pumped
through the heat exchanger (3),
characterized in that
the control device (8) and the pump (1) transporting the
waste water adjust the waste water throughput through the
heat exchanger (3), and the control device (8) and the pump
(4) disposed in the circulation loop of the reservoir (16)
adjust the reservoir water throughput through the heat
exchanger (3) to one another, and control or adjusts the
same to a mass ratio, or to a throughput ratio, or to a flow
velocity ratio of between 0.8 and 1.2, preferably of about
1:1.

PCT/AT92/00125
-15-
2. The system according to claim 1, characterized in that
the sensor (6) in the discharge line (10') is disposed
upstream of the connection of the suction line (11) of the
forced-flow pump (1).

3. The system according to claim 1 or 2, characterized in
that a cyclone separator (2) is disposed between the pump
(1) and the heat exchanger (3) for separating air conducted
with the waste water.

4. The system according to claim 3, characterized in that
for the purpose of air discharge from the cyclone separator
(2) and for pressure adjustment of the waste water exiting
the cyclone separator (2) a vent line (16) issuing from the
upper end of the cyclone (2) is closable with a ventilation
flap (13) which is adjustable with the water level in the
cyclone (2), for instance by means of a float (12).

5. The system according to one of the claims 1 to 4,
characterized in that temperature sensors (5) are provided
for determining the temperature of the waste water and the
storage water flowing into and out of the heat exchanger
(3), particularly in the immediate vicinity o* the
corresponding connections (30, 31, 32) of the heat exchanger
(3), which temperature sensors (5) are connected to the
control device (8), with which the throughput amount or the
throughput flow velocity of the pump (1) and/or of a pump

PCT/AT92/00125
-16-
(4) disposed in the circulation cycle for the storage water
are controllable in dependence of the measured or calculated
temperature differentials (.DELTA.T) between the inlet (30) at the
heat exchanger (3) for the waste water and at the outlet
(33) for the storage water and/or at the inlet (32) for the
storage water and at the outlet for the waste water (31).



6. The system according to one of the claims 1 to 5,
characterized in that a pipe section or a tie-in unit (10)
is provided which can be inserted into a conventional waste
water line (10'), in which the waste water sensor (6) is
disposed and into which the suction line (11) of the pump
(1) issues and downstream thereof the waste water discharge
line (14) of the heat exchanger (3).

7. The system according to claim 6, characterized in that a
downwardly projecting flat pan or bulge (26) is formed in
the lower region of the pipe section or the tie-in unit (10)
into which the pipe (11) reaches which leads to the pump
(1).

8. The system according to claim 6 or 7, characterized in
that the flat pan or bulge (26) is separated from the volume
of the pipe section or tie-in unit (10) by means of a filter
or filter sieve (15).

PCT/AT92/00125
-17-
9. The system according to one of the claims 1 to 8,
characterized in that the pump (1) is disposed in the
housing (18) in front of the cyclone separator (2).

10. The system according to one of the claims 6 to 9,
characterized in that the waste water is supplied to the
suction line (11) of the pump (1) through a filter or a
filter sieve (15).

11. The system according to one of the claims 6 to 10,
characterized in that a further water sensor (6') for
detecting waste water which flows over the filter (15) and
which has not been drawn off is provided in the tie-in unit
or in a pipe section (10) downstream of the suction line
(11) and of the filter (15), which further sensor (6') is
connected to the control unit (8), with which the pumping
direction of the pump (1) is reversible for a certain period
of time in the case of a corresponding signal for flushing
the filter (15) with already aspirated waste water.

12. The system according to one of the claims 3 to 11,
characterized in that the air ventilation line (16)
connected to the upper end of the cyclone separator (2)
issues into the tie-in unit or into the pipe section (10)
upstream of the suction line (11) for the pump (1).

13. The system according to one of the claims 1 to 12,
characterized in that the tie-in unit (11) is disposed at a

PCT/AT92/00125
-18-
lower level than heat exchanger (3) and the water heater or
the warm water reservoir (16).

14. The system according to one of the claims 1 to 13,
characterized in that the interior of the heat exchanger (3)
is provided with turbulence inducing devices or whirling
chambers for preventing grease deposits.

15. The system according to one of the claims 8 to 14,
characterized in that a fabric sieve filter is used as a
filter (15) with a permeability of 50 - 200 µm, preferably
of about 100 µm.

16. The system according to one of the claims 6 to 15,
characterized in that the pipe section or the tie-in unit
(10) is disposed at a level below the housing (18).

Description

Note: Descriptions are shown in the official language in which they were submitted.


. WO 93/07424 212 0 S 2 6 PCT/A~92~00125

--1--

System for Recovering Heat from Waste Water



The invention pertains to a system for recovering heat ~rom
waste water which arises, preferably discontînuously, from,
in particular, households, houses, commercial ente ~ rise~,
etc., which include~ at least ~ counter-flow heat exchanger
~hrough which the waste water flows, and which is con~ected
in the circuit of at least one warm water reservoir or a
water hea~er.



Such sy~tems for recovering heat from waste water are
generally known.



It is th~ object of the i~vention to further develop such
3y8tems such that they are enabled to process all h~usehold-
conventional waste watérs in chemically and mechanically
clean or s~lightly soiled form a~ well as in strongly soiled
orm, i.e. when soap,~ grease, hairs, detergent~, chemical
~: ~ clean~ers~ ood leftovers, etc. are contained in the waste
wat r. Further~or~, uch:a system should operate fully
aut~matically, ~hould be largely m~intenance-fr~e, it should
~ be~prQvldcd~in a~structurally simple apparatus with a
:~ : 20~ buil*-in unit:concept,~and~t should have a degree of
efficiency as~ high as possible.




; These ob~ects are ~ttained, in accordance with the
invention, with~a~system of:the foregoing kind in that a




: ~ :


, , . ., ~ ,

. . Wo 93/07424 PCT~AT92/00125
-2- 2120~26
~ensor i~ provided in the discharge line for the waste water
which is responsive to incoming waste water, which sensor is
connected to at least one pump or to a control device
controlling the pump(s), with which waste water is drawn off
when the pump is turned on upon the occurrence of a signal
indicating ~urther waste water in the waste wate~r_line~which
is then guided or pumped through the heat exchang~r.



In a preferred embodiment it is envisioned that tempera~ure
sensors are provided for determining the temperature o~ the
waste water and the storage water flowing into and from th~
heat exchanger~ particularly in the immediate vicinity of
~he corresponding connections of the heat exchanger, which
tempera~ure sensor~ are connected to the control device,
with which the amount of the velocity o~ throughput of.the
pump and/or the pumping amount of the pump in the loop *or
the storage water can be controlled in dependence of the
measur~d:or calculated te~perature diference between th~
inlet at the heat exchanger for the waste water and the
~:~ outlet ~or ~he ~torage water and/or at the inlet for the
s~orag~ water:and at the o~tlet for the waste water~



A fuxther ad~antageous embodiment is characterized in that a
: ~ pipe~ection orlan a~sembly unit i~ pr~vided ~or connection
in~a co~ventional waste water line in which the waste water
~` sensor(~) are disposed and with which the intake line of the
pump or the waste wa er outlet line (downstream) of the Xeat
ex~hanger communicate.




.

'W0 93/07424 212 0 5 26 PCT/AT92/00125
--3--


With the sensor which registers the occurrence o~ water, the
pump is always turned on when waste water is available for
processing; when the water ~tops, the pump is turned offO
Due to the controlled supply of the warm waste water and the
controlled ~upply of the stora~e water to be heat~d to the
heat exchanger, optimized heat exchange is enabled, so that
~he heat content o~ the waste water can be optimally
utilized. Finally, the ~y~tem can be delivered in the form
o a compact unit, which is aonnected between a water heater
and a waste water line which is easily connected into the
waste water pipe~

.

Pr~ferrad embodiments can be found in the following
description, in the drawing and in the patent claim~.



The drawin~ depiots a schematic CQnstruction of the syst~m
according to ~he invehtion.



he system a~cording to the invention is essentially divid~d
into~th~ee~individual ~omponents, namely a wat~r haater 17,
a main:unit,;which is schematically re~erenced at 18, and
tie-in unit~10~




20~ : The water haater 17 inaludes a cold water supply line 19 and
a: line~ 10 le~ding the a user. An arbitrary heating de~ice,
or instance~electrical heating rods, are indicated at 2~ in
the upper~region of the watér hPater. ~he feed to the line
20 leading to ~he users is effected via a motor mixer 70 ts



:~:

:

W0 93/07424 212 0 5 2 fi P~T~AT92/00125
-4
which a hot water conducting line 22 and a line 23
conducting water heated by the waste water. The temperature
in the line 20 is sensed by means of a temperature probe S
and it is evaluated with a control de~ice or a control
compu~er 8; the motor mixer 7 is also controlled~wi~h the
control device 8.



A further essential device is the tie-in unit 10 which can
be inserted into any arbitrary waste water pipe or a w~ste
water line and which has a corresponding cross-section
adapted to that of the non-illustrated was~e water line. The
main unit 18 includes as essential components the control
unit 8, a cyclone 2, a pump 1, a heat exchanger 3, a further
: pump 4 and possibly a check val~e 9.



The ~ie-in unit 10 has a downwardly directed recess or a
:: bulge 26, into which a suction pipe ~1 opens which leads to
the pump lr q~he bulge ~6 :is closed off on top with a filter
or: a filter si~ve 15;: so that waste water entering the
tie-in unlit ~lO: ~lows through the filter 15 in orde~ to reach
the suction opening OI the line 11 and it is prsfiltere~ in
tha~way. ~ctually, the~lines, sensors and components whi h
form the~tie-in~}unit:lO could aiso be formed or disposed in
a~waste wa~er line. ~: ~


:: ~ : :
The warm waste water aspirated by the pump 1 is supplied_
.into the cyclon 2 in which a float 12 is disposed which
aarries a rod 27 at its upper side, with which a ventilation

'WO 93/07424 2 1 2 0 5 2 ~ Pc~/AT92/ool25
--5--


flap 13 for a ventilation line 16 can be adjusted. Dep~nding
on the amount of air aspirated with the waste water in the
line 11, the water level 28 in the cyclone 2 rises or falls;
while the water level 18 rises, the ventilation flap 13 is
closed; when the flap 13 is open, air is fed bac~ via the
line 16 to the tia-in unit 10, i.e. to a location upstream
of the suction line 11, so as to maintain the incoming waste
water at temperature by means of the v~ry warm air and so as
not to waste the heat content in the air. ~he pres~ure of
the waste water in the cyclone s~parator 2 is controlled
with the float -12 and the ventilation ~lap 13, whiah waste
water is fed through a line 29 to a corresponding ~upply
connector 30 in~o the heat exchanger 3 and w~ich leaves the
~heat exchang~r at 31 through the line 14. The line 14 issues
into th~ ti~-in unit downstream of the filter 15; it is
pos8ible to proYide a pipe 32 in order to introdu~e the
returning,~cooled~waste water into the tie-in unit as far
from the suction line 11 as possible, and to prevent a~y
: back~low.



0:~ ~h~ heat exah~nger~is~further supplied with cool water at a
supply~openin~ 32, which water is withdrawn from the lower
part Qf:~the wat~r:heater 17, or'with cold~water from the
line 19 Yia a pump 4~ Tha~ water which ~lows ~hrough the
heat: exchanger lea~es the same at the ou~let opening 33 and

:: : ~ `: : :

it reaches the upper part of the water heater ~7 through_a

: lin~25 and: the cheok valve 9, whereby a stra~i~ication of

W0 93/07424 212 0 5 2 ~ PCT~AT92~00125



the water forms in the water heater 17 according to its
temperature.

In accordance with the withdrawal of warmed water ~rom the
water heater 17 through the line 20, cold water ~an flow in
through the cold water line 19 into the heat exchanger 3 or
into the water heater 17, i.e. into its lower part~



The control device 8 is connected to water sensors 6, to
temperature sensors 5 and to the pumps 1 and 4O ~he water
sensor 6 ups~ream of the suction line 11 serves to detect
incoming waste water and, upon receiving a corresponding
signal from the senso~, the control device 8 places the pump
1 into operation for drawing off the available waste water.
: The temperatur~ o~ the waste water is simultane~usly
measured with ~he appropriate temperatur~ probe 5.



A water ~eel~r 6' is disposed downstream o~ the suction line
11 with whiah it is det~rmined whether waste water ha~

:
: tr~v~rsed ~cros~ the filt~r 15 while the pump 1 operated; if
:~ this is affirmatîve~ it is an indiaation that the filter 15
is plugged up~ In that case, the control device 8 re~erses

.

~1 20~ ~he:pumpi~g direction o~ the pump 1 and pushes already
:
aspirated water through the line 11 into the ~ulgQ 26 and
thereby flushes the:filter 15 counter tv its filtering
direct~ion~ so as to provide free passage for the waste water
in_o t~e bulge 26 for aspiration through the line 11; the
flushing is maintained for a period of time, so as to allow


WO 93/07424 212 0 5 ~ 6 PCT/~T92/00125
--7--


the f lushed~out dirt to be removed, th t is to say that
after the flushing, waste water is not immediately aspirated
again, but instead it is used for removing the flushed-out
dirt .



The control device further monitors the temperatures ~t the
inlets 30 and 32 of the heat exchanger 3 and/or at its
outlets 31 and 33. The control device forms the difference
of the temperature values at the heat exchanger ~r D~ean~; of
appropriate calculation units, i.e. the difference at the
10 inlet 30 for the waste water and at the outlet 33 ~or warm
water and/or th difference at the outlet 31 for waste water
and at th~ inl~t 32 for cold water from the water heater 1
:: or the cold water line 19.



ne te~pe~ature dif ~Eerentials ~T at the respecti~e inlet~;
~nd outIets is a measure for the heat krans~er from the warm
waste w~te:r to the cool wate:r 8upplied from the water heater
17 or ~Erom t:he cold water li~ 19. The tem~eratuxe
diffe~en~ials ~thus d~termined are preferably maintained
equal; ~or~ ~hat purpose: it i5. provided that khe am~:sunt of
20: warm waste water and the amount of ool water fl~ing
througlh the water heater~correspond to ona another in terms
: o~ volume. The~cor~esponding volumes aan be adjusted by
controlling he pump~1 and/or the pump 4, in that ths

: ~ throughp~t o~ the wasta water and/or of t~ cool water is
regulate~, *or the purpose o~ mutually adjusting th~ amounts
of water circulating through the heat exchang~r in ~he




:

W0 93/07424 21 2 0 5 2 ~ PcT/AT92/ool25
--8--
respecti~e divisions for waste water and for cc)ld water per
unit time.



The measurement of the 1:emperature dif ferences ~T is
pra::tically done with t:wo differential controllers, for
instance with PID properties, whose voltage values are
processed by the control device 8.



The tie-in unit 10 se~fes several functions; it serves to
withdraw the wa~:te water flowing in the discharge pipelines,
as we~l as the back~eed thereo~ after the heat exchange
10 proc:ess~; furthe~ore, the air is disposed of through this
c:onnector segment 10 which had been aspiral~ed.



Nagnetically inductive sensors may be provided fc3r detecting
.
wat~r supply ~and the water temperatures.



q~he dimensions of the entire tie-in unit 10 are aimed at a
imple assQmbly into,existing discharge pipes; the maximum
built-in depth ~below the discharge level, :IEor instanGe, iE;
about 2 cm; connec~tor~ are pro~ided in the tie-in unit for
th~ entry of~ wasts water:, for the diss:~h~rge o:E waste water,
Eor~ a æuc~ion cc::nnection to the`main unit, and for a water

rel:urn a~ r the heat exchang~ proces~; as well a~ ~or an air
return~



The main unit 18 can be conf igllred as a built-in uLnit, so
that an unproblematic: assembly into, for instance, kitchen


,

,

. s W0 93/07424 212 0 5 2 6 PCT/AT92/00125
_ g _
cabinets below an exist'ng counter is enabled; the housing
measurements correspond *o the usual norm for household
appliances o~ ~0 x 60 cm and are easily attained. The main
unit 18 also allows for the necessary operational management
which is required in order to withdraw a maximum in heat
energy from the soiled waste water and thus to warm up the
cold fresh water.



The assembled system components are acoustically dampened
and built into th~ main unit; connectors exist compatibls
with the tie-in unit~ -




~he pumps 1 and 4 provided in the ~ain unit 18 can be~orce-feeders and they are pre~erably infinitely ~ariable,
:~ so as to assure corresponding control response.
: :

~rhe water reservoir or water heater 17 is preferable loaded
by the main unit 18 under consideration Qf the heat
strati:fication:~in the: uE~?er third of i*s volume; reheating
with the rsheating deYice 21 is preferably effected in the
~up~er~third o~f the:wa~er heater 17.



For ~ptimizing the~degree~of ef~iciency of the system, the
,
20~ eleotronically controlle~ three-way mixer 7 adjusts the

withdrawal:temp~ra~ure onto a rated value; this concept
leads to ~he ~act tha~, when any arbitrary amount of warm
wa~er is withdrawn ~hro-~gh the line 20, an e~ual amount of
fresh cold water flows into the water heater 17 fro~ below,




~ ;
: :

WO 93/07424 212 0 ~ 2 ~pCT/AT92/00125

--10--
which again leads to a cooling of the entire amount of waste
water during ~he heat recovery to the temperature level of
the fresh water and corresponding hea~ recovery.



~hen waste water arriv~s in the tie-in unit 1~, the arrival
is de~ermined by means of the magnetic inductiYe feeler 6
and tha t~mperature is measured with the sensor 5~ From
these measured values the control de~ice 8 in the main unit
18 forms a ~tartoff argumentO In the case of a start, the
entire amount o~ waste water is drawn o~ through the
backflushable ~ilter sieve 15 by means of the pump 1, The
air which i~ necessarily conducted from the disch~rge system
in this proces~ ~s well disturbs for various reasons,
because when the system is at a stillstand this can lead ~o
incrustation fro~ dried dirt. Also, water with detergent
foams vexy sltrongly ~ Iring the wi~hdrawal suation from the
ewer, especially when air is present. A water-air mixture
:
(foam~ ha~; an entirely different specific heat capacity a~
c:c~mpared to wat:er alone,: which would make the control o~ ~he
throughput in the h~at exchan~er 3 or the ~Ere~hwater pu~p 4
very difficult in terms of :a~taining equal flow speeas for
wa~te water and :~Eresh water in the heat exchanger 3O

In order to realize the separation o~ water and air
effQctively,: fast, and withou~ large voIumes of re~;t water
which would ac~ol d~wn during stillstand and thus reduce the
fficiency o~ ~he system, we h~ve E,rovlded the relati~ely
.
::~ small cyclone separator ~ with correspondiny dimen~ions. The
: ~ .

212052G
~W0 93/07424 PCT/AT92~00125



~loat-controlled ventilation or hinged valve 13 leads to a
pressure at the heat exchanger 3 which corresponds ~o the
throughput volume (air and water~ of the pump 1, or to the
water level in the cyclone 2, which conducts the wast~ water
through the w~ste water part of the heat exchanger 3. The
the water level rîses, this is an indication of a flow speed
through the heat exchanger 3 which is too low, so that the
pressuxe in the cyclone 2 should be raised, for which
purpose the ventilation opening of the cyclone 2 is closed
with the flap 13 by means of the rising float 12 7 The water
l~vel could also be measured with the control device 8 and
the air ventilation could be controlled accordingly.



The construction of ~h~ heat exchanger 3 is ~uch that
designed partial turbulences are c~used th~rein ~hich
absolutely prevent ~he deposit of grease and similar
impurities present in the waste water during the cooling
process, even if no grease solven~s are present in the waste
water.



The cooled-down was~e water and the air from ~he v2ntilation
20~ are conduc~ed bac~ to the tie-in unit lO and thus ~o the
sewage; ~yst~m;~air and water are separately conducted so as
not to have to settle for an efficiency loss in ~he case of

a:~mall amoun of waste water per unit time (a lot o~f air is
:~ condu~ted), since the air produced in the ventilation
::~ contains heat which would be los' if it were conduct~d back
~ together with the coolded-down waste water.

::
~:
~ .

~W0 93/07424 212 n 5 2 5 PCT/AT92/00125
-12-
The cleaning of the filter sieve 15 is provided so as to
maintain this filter sieve pervious, which becomes soiled at
variable intervals; bath water hardly soils a filter sieve;
w~hing machine water soils relatively quickly due to the
lînt contained therein. As soon as the filter si~e besomes
impervious to the waste water, the same is bypassed, leading
to the presence of water in the tie-in unit 10 i~mediately
downstream (as seen in the direction of flow) of the filter
sieve 150 The ~urther water det~ctor 6' placed at that
location sends a corresponding signal.to the control device,
which then reverses the pump 1 for a shor time with regard
to i~s-pumping direction and thus effects an extremely
e~fective backflushing of the ~ilter sieve 15, whereby the
bac~lushed water is discharged through the tie-in unit 10
a~d conducted into the sewer~A short st~p of ~he suction,
: i.e. o~ the pump 1, p~ior to a renewed start in the normal
conYey~ ng di~rection of the pump 1 allows the dirt to flow by
the ~iev~ 15 together wi~h the waste water simultaneously
wing through the tie-in un:it 10, which prevents the

:: 20 :~lushed-out impurit~eæ :Erom being re-aspirated right away
~ and~rom plugging the ~ilter 15.

~ . :
T~e total degree of efficiency Of the system in cooperation
wi~h the di~fering and~mu~ually ind:ependent w~rm water
withdrawal ahd discharge amounts occurring in a household,

as-well: as the instants and tim~ intervals thereof, c:an .Q.nly
be optimized when the amount~ of discharg~n~ w~ste water and
freshwater to be heated are adapted to one another, and are



.

.. .. ... .. .. ..

`W0 93/07424 212 ~ 5 2 6 PCT/AT92/00125
-13-
pre~erably equal, since that assures optimal heat tr~nsfer
and optimal heat recovery. In order to fulfill this
re~uirement, the control device measures all temperatures at
the heat exchanger 3, which is operated in counterflow, and
controls the infinitely adjustable pump 1 and/or ,~he pump-4
in a manner such that a preferably equal absolute
temperature differential Q~ results between the measurement
points 30 and 33 for the warm waste water and the warm ~resh
water, as compared to the measurement points 31 and 32 for
the cold waste water and the cold fresh water~



The equilibrium of the amounts of water is attained
virtually perfectly by controlling the flow velocity; the
:~ diameters of the ~ipes and of the heat exchanger are known,
~o that the~flow v~locity (i.e. ~he water pressure3 is the
only par~meter to be controlled.
:
~: The spring-biased check~valve 9 tied into ~he feed line 25
~: to~the water heater, pri~vents an unwanted circulation
through the usable~water~part o~ the syst~m which i~

, ~ : .
connected in ~he by-pass~configuration with the water

20~ heater;~ Guch circulation~would destroy the ~tratification in

: the wat~r:heater ~7:during stil~stand and an unde~ireable

admixing of cold water~duri~g a withdr~wal of warm water.




~arious sie~es or~sieY2 materials may be utilied for the_
~,
filter sieve 17, for instance ~abric sieves with d mesh

width of about lOO:~m.

~ ~ .

Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

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Administrative Status

Title Date
Forecasted Issue Date Unavailable
(86) PCT Filing Date 1992-10-02
(87) PCT Publication Date 1993-04-15
(85) National Entry 1994-03-31
Dead Application 1998-10-02

Abandonment History

Abandonment Date Reason Reinstatement Date
1997-10-02 FAILURE TO PAY APPLICATION MAINTENANCE FEE

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1994-03-31
Maintenance Fee - Application - New Act 2 1994-10-03 $50.00 1994-09-15
Maintenance Fee - Application - New Act 3 1995-10-02 $50.00 1995-09-18
Maintenance Fee - Application - New Act 4 1996-10-02 $50.00 1996-09-20
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
BARTL, EGMONT
Past Owners on Record
None
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
International Preliminary Examination Report 1994-03-31 23 507
Cover Page 1993-04-15 1 29
Abstract 1993-04-15 1 99
Claims 1993-04-15 5 287
Drawings 1993-04-15 1 43
Representative Drawing 1998-07-22 1 12
Description 1993-04-15 13 811
Fees 1996-09-20 1 37
Fees 1994-09-15 1 36
Fees 1995-09-18 1 29