[0001] The present invention relates to a method of cleaning the housing of a pump, especially
a drain pump of a household water batch purification unit, according to the preamble
of Claim 1.
[0002] According to such a method, liquid is led through the pump housing in order to remove
the solid matter that accumulates in the housing.
[0003] The present invention also relates to a pump arrangement according to the preamble
of Claim 9.
[0004] The pumps which are used in batch purification units operate in environments comprising
liquid and solid matter. Solid matter easily accumulates in particular in the pump
housing, which may be detrimental to the operation of the unit, and usually there
is no desire to carry the solid matter forward from the pump. This is the case when,
for instance, water which has been purified in the batch purification unit is removed
from the unit. When the pump, in which solid matter has been accumulated, is started
up, it pumps out this solid matter, too. When the quantities of liquid which are thus
expelled are small, this solid matter remaining inside the pump increases significantly
the amount of impurities.
[0006] Publications
JP 2004351400 and
JP 20001271782 describe pumps with which it is possible to continuously separate water from a sludge
which comprises solid matter. However, these solutions are expensive, complicated
and difficult to apply to batch purification units.
[0007] The purpose of the present invention is to eliminate problems associated with the
known technology and to generate a completely new solution especially for cleaning
solid matter from the drain pump of a batch purification unit during the operation.
[0008] The present invention is based on the principle that the housing of the drain pump
is flushed with an aqueous suspension which is led through the housing and which comes
from a flushing tank, which tank operates as a buffer.
[0009] In this case, before the flushing, the flushing tank is filled by using the drain
pump to pump an aqueous suspension into that tank, in order to simultaneously remove
from the pump housing at least part of the solid matter inside that housing. Most
suitably, the volume of the aqueous suspension to be pumped into the tank is at least
as great as, preferably greater than, the volume of the housing of the drain pump.
[0010] The present invention also creates an arrangement of the drain pump for a batch purification
unit, which arrangement comprises a pump with an outlet pipe and which is connected
to the process tank of the batch purification unit, whereby it possible to remove
the aqueous suspension, which is generated in the process tank, from the batch purification
unit through the outlet pipe of the pump. According to the present invention, a flushing
tank is arranged above the pump, in vertical direction, and it comprises an outlet
and an inlet, the inlet being connected to the outlet of the pump. The tank acts as
a buffer for the draining and its volume is at least as great as the volume of the
draining pump, in which case it is possible to pump, through the outlet of the pump
and the inlet of the tank, a volume of liquid which is equivalent to the volume of
the entire pump housing.
[0011] More specifically, the method according to the present invention is mainly characterized
by what is stated in the characterization part of Claim 1.
[0012] The pump arrangement according to the present invention is, in turn, characterized
by what is stated in the characterization part of Claim 9.
[0013] Considerable advantages are obtained by means of the present invention. Accordingly,
the solution presented here makes it possible to flush the pump at required intervals.
The solid matter remaining inside the pump can be removed efficiently, in which case
it is possible to avoid solid matter from migrating into the purified water.
[0014] In the following, the present invention will be examined more closely with the help
of a detailed description with reference to the accompanying drawings.
Figure 1 shows the principle structure, viewed from the side, of a waste water purification
unit which operates using the batch principle;
Figures 2a and 2b show the structure of a pump arrangement which is equipped with
a flushing tank, where Figure 2a is a perspective drawing of the solution, and Figure
2b, a partial cross-section of the solution viewed from the side.
[0015] As seen from above, in the solution according to the present invention, the housing
of the drain pump of a batch purification unit is cleaned by regular back-flushing.
By flushing, it is possible to ensure that detrimental quantities of solid matter
do not accumulate in the pump, which matter would be removed along with the liquid
when the pump is started.
[0016] The action described above can be carried out once or it can be repeated several
times, until the pump housing is essentially cleaned of solid matter. After that,
it is possible to remove water from the batch purification unit through the flushing
tank without any solid matter from the housing of the pump migrating along with the
reject.
[0017] It is possible to flush the pump regularly during its operation, in which case the
suitable flushing interval varies according to the utilization rate. In practice,
it is enough to flush the pump of a batch purification unit 1-5 times in 24 hours,
or more infrequently.
[0018] The flushing tank, which most suitably is placed above the pump, is filled in pulses
until it is almost full in such a way that solid matter, too, which is in the pump
housing comes to the flushing vessel, after which the liquid/solid matter mixture
is allowed to run back, under gravity, through the pump, thus flushing the pump housing.
[0019] The flushing is carried out when necessary. Generally, the length of the pumping
pulses is approximately 0.1-20 seconds, preferably approximately 0.5-10 seconds, more
preferably approximately 1-3 seconds. The pulse length depends on the output of the
pump and the volume of the vessel! The length of the flushing period between the pumping
pulses is at least 10 seconds, preferably approximately 15 seconds to 5 minutes, and
more suitably at least 1 minute. It is important that the flushing period is long
enough to ensure there is time to remove the solid matter from the pump.
[0020] The lower part of the flushing tank is conical or its surface is otherwise sloping,
and the lower part is connected to the outlet of the pump. Most suitably, the nozzle
of the conical lower part is connected to the outlet pipe of the drain pump, in which
case the aqueous suspension, which is pumped into the flushing tank, flows easily
under gravity back into the pump and is able to flush the housing.
[0021] The flushing tank is dimensioned for instance in such a way that its volume ranges
from 1 to 3 times the volume of the pump, in which case the solid matter can efficiently
be flushed away from inside the pump. On the other hand, it is advantageous that the
volume of the tank is not so great that the filling of the tank and the backflushing
may stir up the clarified sludge in the process tank Accordingly, the volume of the
flushing tank is generally approximately 1-10 times, especially approximately 1-5
times the volume of the pump.
[0022] When the purification unit is operating, purified water which is generated in the
process tank is removed regularly through the outlet pipe. In order to enable the
flushing function described above, the water stream of the flushing tank, that is
the outlet pipe, is located most suitably on the upper edge of the tank, below that
level to which the aqueous suspension, which is pumped to flush the pump, rises during
the pumping pulses.
[0023] The material from which the conical lower part is made can be the same as the rest
of the flushing tank. Preferably, the material is such that solid matter does not
adhere to its surface. Suitable materials are different thermoplastics and other structural
materials which are covered with thermoplastics. The surface of these can still be
separately treated in order to improve the adhesive resistance. Examples of suitable
plastics are polyethylene and polypropylene and other polyolefins.
[0024] The accompanying drawings describe a preferred embodiment of the present invention.
Figure 1 shows the principle structure of a batch purification unit. The following
reference numbers are used in the figure:
- 1. storage tank
1a. engine compartment
- 2. process tank
- 3. junction between the tanks
- 4. input
- 5. transfer pump
- 6. pipe of the transfer pump
- 7. control centre
- 8. level controller of the transfer pump
- 9. aerator trays
- 10. pipe of the aerator trays
- 11. compressor
- 12. process gauge
- 13. chemical pump control
- 14. chemical pump
- 15. chemical hose
- 16. exit pumping pump
- 17. exit
- 18. sludge pump
- 19. pipe of sludge pump
- 20. basket for the surplus sludge
- 21. engine compartment base
- 22. flushing tank
[0025] The purification unit shown in the drawing is designed for purification of residential
waste water. It comprises two main parts, namely the storage tank 1, into which the
waste water to be purified is fed through the input pipe 4, and the process tank 2,
in which the actual purification is carried out by means of activated sludge. The
tanks 1 and 2 are actually separate units, which are connected to each other by a
junction 3. The waste water is pumped from the storage tank 1 into the process tank
2 by the transfer pump 5, which is controlled by the level controller 8. The level
controller triggers the transfer pump when the level of the waste water fed into the
storage tank exceeds a preset limit, in which case the waste water is pumped through
the junction 3 by means of the transfer pipe 6 into the process tank 2.
[0026] In the present application, the control centre 7 of the arrangement, which controls
the operation of the entire unit, is placed in the engine compartment 1a, which is
formed in the storage tank. The reference number 21 stands for the floor of the engine
compartment which divides the storage tank unit into two parts. By placing the control
centre 7, including the engine compartment 1a inside the storage tank 1, the control
centre is effectively separated and isolated from the surrounding space. In addition,
a compressor 11 is placed in the engine compartment, which compressor produces compressed
air which can be pumped into the waste water to be treated in the process tank, via
the aerating pipe 10 and the aerator trays 9, which are placed at the end of that
pipe and below the level of the surface of the liquid. Furthermore, a chemical pump
14 is arranged in the engine compartment together with its control unit 13 and chemical
hose 15. This pump 14 is used for feeding chemicals into the storage tank 2.
[0027] It is evident that the engine compartment can be placed, besides inside the storage
tank, elsewhere, too, and the application described above is only one possible solution.
[0028] Besides the aerator trays/pipe, the process tank of the arrangement comprises the
sludge pump 18, with which it is possible to remove sludge that accumulates in the
lower part of the tank. In order to collect the sludge, a container for the surplus
sludge, i.e. a basket 20 which is connected to the sludge pump through the sludge
pipe 19, is arranged in the storage tank.
[0029] The waste water which is pumped into the process tank is aerated by air which is
led or bubbled into the water through the aerator trays, in which case the sludge,
i.e. activated sludge, which comprises micro-organisms, starts to form in the tank.
Due to the effect of these micro-organisms/microbes the nutrients in the waste water
break up, which nutrients then form gas and disintegration products, which dissolve
in the liquid. The latter settle in the sludge and an activated sludge layer is formed,
while the purified water stays on the top of the layer of activated sludge. This water
is regularly removed from the tank by the exit pumping pump 16. The operation of this
pump is controlled by the process gauge 12. The pump is connected to the flushing
tank 22 which is connected to the exit 17 of the process tank.
[0030] A more detailed pump arrangement of the pump structure according to the present invention
shown in Figure 1 is described in Figures 2a and 2b. In Figures 2a and 2b, the reference
number of the pump is 30, and that of the flushing tank, which is arranged above the
pump, is 31; the lower part 32 of the flushing tank is conical and the inlet pipe
including flanges 33 is connected to the exit 34 of the pump 30. The reference number
of the control unit of the pump is 35 and the reference number of the inlet connected
to the process tank is 40. The outlet pipe 36 of the flushing tank is arranged on
the upper edge of the cylindrical upper part 37 of the tank, immediately below the
end 38, as shown in the figure. In the upper lid of the tank an air bleed valve 39
is arranged, with which it is possible to release the air that is displaced in the
tank by the water which is pumped into the tank (see arrows). Correspondingly, it
is possible via this air bleed valve to bring replacement air into the tank when the
tank is emptied through its conical lower part.
[0031] As seen from above, according to a preferred embodiment, the flushing tank 31 is
in direct liquid contact with the pump 30, because no valve is fitted between the
inlet 33 of the flushing tank and the outlet 34 of the pump. By means of this solution,
the flushing tank is emptied automatically due to the effect of gravity when the pump
is stopped. The stream of liquid that exits from the tank flushes hereby the housing
of the pump.
1. A method of flushing the housing of a drain pump (30) which is connected to the process
tank of a batch purification unit, according to which method
- liquid is led through the housing of the pump in order to remove solid matter which
has accumulated in the housing,
characterized in that
- aqueous suspension is pumped by means of the drain pump (30) into the flushing tank
(31), and
- the aqueous suspension which is pumped into the flushing tank is used for flushing
the housing of the drain pump,
the volume of the aqueous suspension pumped into the tank being at least as great
as the volume of the housing of the drain pump.
2. The method according to Claim 1, characterized in that the aqueous suspension is pumped from the drain pump (30) to the flushing tank (31),
which is placed above the pump, from which tank it is possible to return the aqueous
suspension to the housing of the pump under gravity.
3. A method according to Claim 1 or 2, characterized in that the flushing tank (31) acts as a buffer which prevents the solid matter exiting from
the batch purification unit (1).
4. A method according to any of Claims 1-3, characterized in that the aqueous suspension is pumped by the drain pump (30) in pulses into the flushing
tank (31).
5. The method according to Claim 4, characterized in that the duration of a single pulse is approximately 0.1-20 seconds, preferably approximately
0.1-5 seconds.
6. A method according to any of Claims 1-5, characterized in that the duration of the flushing period is at least 10 seconds, preferably approximately
15 seconds to 5 minutes, most suitably approximately 1 minute.
7. A method according to any of the preceding claims, characterized in that after the flushing period, liquid is removed from the batch purification unit through
the outlet pipe (36) of the flushing tank.
8. A drain pump arrangement in a batch purification unit, which arrangement comprises
- a pump (30) with an outlet (34) and an inlet (40), which is connected to the process
tank of the batch purification unit, and through which outlet (34) of the pump it
is possible to remove from the batch purification unit aqueous suspension obtained
from the process tank,
characterized in that
- a flushing tank (31) is arranged above the pump, which tank has an inlet (33) connected
to the outlet (34) of the pump, and an outlet (36) for the discharge of water, the
volume of the tank (31) being at least as great as that of the housing of the pump
to allow pumping of the entire volume of the pump into the tank in one go.
9. The arrangement according to Claim 8, characterized in that the volume of the flushing tank (31) is approximately 1-10, preferably approximately
1-5 times that of the volume of the pump.
10. An arrangement according to Claim 8 or 9, characterized in that the lower part of the flushing tank (31) is conical-shaped and connected to the outlet
pipe (34) of the pump.
11. An arrangement according to any of Claims 8-10, characterized in that the flushing tank (31) is made of a material to which solid matter does not essentially
adhere.
12. The arrangement according to Claim 11, characterized in that the flushing tank (31) is made of plastic, especially of polyolefin, such as polyethylene
or polypropylene, or of a structural material which is covered with plastic.
13. An arrangement according to any of Claims 8-12, characterized in that an air bleed valve (39) is arranged on the flushing tank (31).
14. An arrangement according to any of Claims 8-13, characterized in that an outlet pipe (36) of the flushing tank is arranged on the upper edge of the flushing
tank.
15. An arrangement according to any of Claims 8-14, characterized in that the flushing tank is in direct liquid contact with the pump, in which case it is
possible to remove the liquid which is fed into the pump automatically by means of
gravity when the pump is stopped.