Information
-
Patent Grant
-
6391122
-
Patent Number
6,391,122
-
Date Filed
Tuesday, November 23, 199925 years ago
-
Date Issued
Tuesday, May 21, 200222 years ago
-
Inventors
-
Original Assignees
-
Examiners
Agents
- Squillante, Jr.; Edward A.
-
CPC
-
US Classifications
Field of Search
US
- 134 221
- 134 2211
- 134 2212
- 134 2214
- 134 2218
- 134 2219
- 134 26
- 134 251
- 134 253
- 134 28
- 134 36
- 134 10
-
International Classifications
- B08B300
- B08B308
- B08B900
- B08B9027
- B08B9093
-
Abstract
A novel cleaning-in-place process is described. The process is one which is segmented, and unused solution is pumped through more than two components of a machine targeted for cleaning, disinfecting or both. The process also results in superior cleaning in shorter cleaning cycles.
Description
FIELD OF THE INVENTION
This invention is directed to a novel cleaning-in-place (CIP) process. More particularly, the invention is directed to a CIP process that is segmented, and surprisingly, does not require solution to be circulated to every component of a machine subjected to water in order to obtain superior cleaning and/or disinfecting results.
BACKGROUND OF THE INVENTION
It is extremely important to clean food processing facilities like breweries, dairy plants and carbonated beverage plants (non-fermentative soda plants). Typically, such food processing facilities are cleaned by subjecting the internal portions of the machines that make up the facilities to a solution that reacts with the various soils present within the machines.
A conventional CIP system, for example, has several storage containers. Each storage container, independently, houses a solution (e.g., pre-rinse solution, cleaning solution, rinsing solution) that is fed (non-simultaneously) into the facility targeted for cleaning or decontamination. Typically, the solutions are pumped into the liquid passages of the machines of the facilities being cleaned and circulated through the machines until they are finally discharged to waste.
Conventional CIP processes are known for employing a pump that circulates a cleaning solution throughout the machines of the facilities being cleaned. During such conventional processes, the unused cleaning solution is fed into no more than two components, regardless of how many components or segments the machine targeted for soil removal has. What this means is that if a particular facility has, for example, carbonated beverage filling machines, conventional CIP processes feed unused cleaning solution into no more than two components of the machine, even if the machine is made up of many parts, like deaerators, storage and mixing tanks, as well as carbonation and cooling tanks. Therefore, only the first two components of the machine receiving cleaning solution are subjected to virgin or unused solution and all other components receive used cleaning solution. Also, conventional cleaning processes are not efficient since every part of the machine gets cleaning solution, even parts like deaerators that are only subjected to large volumes of water.
The disadvantages of cleaning via well known CIP processes is that used soil and contaminant carrying cleaning solutions are circulated throughout the components of the machines being cleaned. Such processes unequivocally result in inferior cleaning. Moreover, conventional CIP processes are not efficient since every part of the machine targeted for cleaning gets cleaning solution, even if the part is one that is only subjected to large volumes of water.
It is of increasing interest to develop efficient processes that thoroughly clean and/or disinfect processing equipment. This invention, therefore, is directed to a novel cleaning-in-place process that is segmented, and surprisingly, results in superior cleaning, disinfecting, or both without the need to circulate solutions through all parts of a machine.
BACKGROUND REFERENCES
Efforts have been disclosed for cleaning processing equipment. In U.S. Pat. No. 5,888,311, a process for cleaning equipment in the absence of a pre-rinse step is described.
Other efforts have been disclosed for cleaning equipment. In U.S. Pat. No. 5,533,552, a CIP process comprising the step of circulating a cleaning liquid throughout equipment targeted for cleaning is described.
Still other efforts have been described for cleaning equipment. In U.S. Pat. No. 5,064,561, a two part CIP system is described and the system utilizes an alkaline material and an enzyme.
SUMMARY OF THE INVENTION
In a first aspect, the present invention is directed to a cleaning in place process comprising the steps of:
a) supplying an unused solution to more than two components of a machine targeted for cleaning, disinfecting or both;
b) generating spent solution; and
c) removing said spent solution through at least one outlet of the machine.
In a second aspect, the present invention is directed to a cleaning in place process comprising the steps of:
a) supplying an unused solution to more than two components of a machine targeted for cleaning, disinfecting or both;
b) generating spent solution; and
c) removing said spent solution through at least one outlet of the machine
wherein the unused solution is not supplied to a part of the machine that is only subjected to water and holds more than about 5.0% of the total volume of solution in the machine, and no more than about 5.0% of the spent solution generated is mixed prior to exiting the machine.
In a third aspect, the present invention is directed to a cleaning in place process comprising the steps of:
a) pumping through at least one CIP unit an unused solution to more than two components of a machine targeted for cleaning, disinfecting or both;
b) generating spent solution; and
c) removing said spent solution through at least one outlet of the machine.
Percent (%), as used herein, means percent by volume based on the total interior volume of the machine targeted for cleaning, disinfecting or both. Unused solution, as used herein is defined to mean solution that has never been used, or solution that has been used and subsequently cleaned (e.g., cleaned, filtered) to substantially its unused form, or a mixture thereof.
BRIEF DESCRIPTION OF THE DRAWING
The subject matter which is regarded as the invention is particularly pointed out and distinctly claimed in the concluding portion of the specification. The Invention, however, may be best understood by reference to the following description taken in conjunction with the accompanying drawing figures in which:
FIG. 1
is a schematic drawing of a carbonated beverage filler machine being subjected to a conventional CIP process.
FIG. 2
is a schematic drawing of a carbonated beverage filler machine being subjected to the superior CIP process of this invention.
FIG. 3
is a schematic drawing of a carbonated beverage filler machine being subjected to the superior CIP process of this invention wherein more than one CIP unit is employed.
FIG. 4
a
is a schematic drawing of a carbonated beverage machine being subjected to a conventional CIP process and
FIG. 4
b
is a schematic diagram of a carbonated beverage machine being subjected to the superior CIP process of this invention, both of which are discussed in the example.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to
FIG. 1
, a schematic drawing of a carbonated beverage filler machine being subjected to a conventional CIP process
10
is shown. The CIP unit (pump in combination with unused solution storage tank)
12
pumps, for example, unused cleaning solution (not shown) to a divert panel
14
by way of a pipe or conduit
16
. The divert panel
14
diverts the cleaning solution to a dearator
18
and a syrup recovery tank
20
via divert panel exit conduits
22
. The dearator
18
may also comprise a dearator pump
24
having pump conduit
26
to circulate spent cleaning solution (not shown) within the dearator
18
. The CIP unit pumps spent cleaning solution out of the dearator
18
to the water bowl
30
and out of the syrup recovery tank
20
to the syrup bowl
28
. The spent cleaning solution is carried from the dearator
18
to the water bowl
30
via the dearator outlet
32
and from the syrup recovery tank
20
to the syrup bowl
28
via the syrup recovery tank outlet
34
. The syrup bowl
28
and water bowl
30
may also comprise a bowl pump
36
with bowl pump conduit
38
to circulate or drive resulting mixed spent cleaning solution out of the syrup bowl
28
and water bowl
30
. The spent cleaning solution is then pumped to the carbonator
40
from the carbonator inlet conduit
42
. From the carbonator
40
, the spent cleaning solution is pumped via carbonator pump
44
to the filler
46
by way of the exit conduit
48
. The spent cleaning solution then exits the filler
46
and is returned, via filler exit conduit
50
, to the CIP unit
12
.
As can be seen from the conventional CIP process described in
FIG. 1
, only the syrup recovery tank
20
and the dearator
18
receive unused cleaning solution. However, the dearator
18
is only subjected to water during the normal bottle filling process. Thus, the conventional CIP process is inferior and inefficient since a very high liquid volume part of a machine, the dearator
18
(about 30% of the machine's volume) which is only subjected to water, is loaded with unused cleaning solution. The spent cleaning solution exiting the dearator
18
is then mixed with spent cleaning solution from the syrup recovery tank
20
after the dearator
18
and syrup recovery tank
20
feed spent cleaning solution to the water bowl
30
and syrup bowl
28
, respectively. The resulting mixture of spent cleaning solution (about 40% of the total volume of spent cleaning solution mixed within the machine) is then continued to be used for cleaning. From the syrup bowl
28
and water bowl
30
, spent cleaning solution is fed to the carbonator
40
and filler
46
, both of which are high volume (collectively, about 50% of the machine's volume), have high levels of soil, and are only subjected to spent cleaning solution. The end result, therefore, of the conventional CIP process is equipment having been subjected to an inferior cleaning process. Such a conventional process is inferior because largely soiled parts of the machine targeted for cleaning are subjected to spent (used) cleaning solution. Also, conventional processes take long because all components of the machine are subjected to solution.
Referring to
FIG. 2
, a schematic diagram of a carbonated beverage filler machine being subjected to the superior CIP process
54
of this invention is shown. A CIP unit
56
pumps solution (not shown) to a divert panel
58
by way of a pipe or conduit
60
. The divert panel
58
diverts the unused cleaning solution to a syrup recovery tank
62
, a syrup bowl
64
, a water bowl
66
and a filler
68
via divert panel exit conduits
70
. Therefore, in the superior process of this invention, more than two components of a machine are fed unused solution that cleans and/or disinfects the machine. As can be seen from
FIG. 2
, the superior process of this invention takes used solution from the syrup recovery tank
62
to the CIP unit
56
by way of the syrup recovery tank outlet
72
. Used solution from the filler
68
is taken to the CIP unit
56
via the filler exit conduit
74
. Moreover, used solution exiting the syrup bowl
64
and water bowl
66
exits the same via pump conduit
76
which feeds used solution through a carbonator inlet conduit
78
to a carbonator
80
. From the carbonator
80
, used solution is delivered to the CIP unit
56
by way of the exit conduit
82
. Therefore, as a result of the superior process of this invention, components only subjected to water and holding more than 5.0% of the total volume of fluid in the machine (e.g., dearator) are not fed solution. Also, no more than about 5.0%, and preferably, from about 0.01% to about 4.5%, and most preferably, from about 0.02% to bout 1.0% of the spent solution generated is mixed prior to exiting the machine. As used herein, spent solution is defined to mean solution having passed through a component of the machine being cleaned (e.g., a syrup recovery tank), excluding conduit.
As can be seen from the present process, cleaning, disinfecting or both is faster because large components of the machine subjected only to water are not fed solution and all components being cleaned with unused solution are being subjected to unused solution at the same time. Also, cleaning, disinfecting or both is better than conventional processes because substantially less spent solution is circulated in the machine being cleaned. The pumps
84
depicted in
FIG. 2
are for illustration purposes and optional. Preferably, the pumps
84
are used, and most preferably, each pump
84
is positioned after a component (e.g., a carbonator).
In
FIG. 3
, a schematic diagram of a carbonated beverage filler machine being subjected to the superior CIP process (with preferred embodiment)
86
of this invention is shown. In the preferred CIP process, a second CIP unit
88
is used to independently pump unused solution (not shown) to a syrup recovery tank
90
. Therefore, the second CIP unit
88
pumps unused solution only to the syrup recovery tank
90
, and all other components that receive unused solution are fed the unused solution via an independent CIP unit
92
.
The solutions which may be used in the process of the present invention are limited only to the extent that they are the type of solutions used to clean and/or disinfect machines of processing facilities, like breweries, dairy plants and carbonated beverage plants. Such solutions may generally be classified as cleaning solutions, disinfecting solutions, cleaning and disinfecting solutions or rinsing solutions. The cleaning solutions, for example, that may be used in this invention include phosphoric acid comprising detergents, and detergents comprising mixtures of inorganic and organic acids. The former are sold under the name of Elevate and Sentol and the latter is sold under the name of Super Dilac, all of which are made commercially available by DiverseyLever. Other cleaners which may be used in the superior process of this invention include enzymatic cleaners sold under the name of Diver Silver and alkaline cleaners sold under the name Divo-Flow, both of which are made commercially available by DiverseyLever.
The sanitizers which may be used in this invention include bleaches, sold under the name of Dibac and Diversol, organochlorine donors sold under the name of Antibac and Multi-Chlor, iodine donors sold under the name Divosan MH and Accord II, acid anionics (e.g., phosphoric acid and dodecylbenzene sulfonic acid) sold under the name of Demand, Dividend and Per-Vad, and peroxyacetic acid based sanitizers sold under the name of Divosan Activ. Sanitizer and cleaning agents may also be employed and they are sold under the name of Divosan DB and Divosan X-Tend, all of the above are made commercially available by DiverseyLever.
The preferred sanitizer and cleaning agents that may be used in this invention are further described in U.S. Pat. No. 4,715,980, the disclosure of which is incorporated herein by reference.
The most preferred solution that is used with the superior process described herein is a cleaning in place solution comprising a halogen dioxide. The preferred halogen dioxide is chlorine dioxide and such a solution is further described in Application Ser. No. 09/447,644 filed Nov. 23, 1999, commonly assigned to DiverseyLever, the disclosure of which is incorporated herein by reference.
The rinsing solutions which may be used in this invention include water, as well as aqueous solutions comprising low foaming surfactants like fatty acid or alcohol condensates made available by ICI surfactants, Henkel, Shell Chemical Company and BASF. Many of these surfactants are sold under the name Neodol®, Plurafac® and Dehypon.
The superior process of the present invention typically circulates solution through the machine targeted for cleaning, disinfecting or both at a rate (linear velocity) from about 1.5 to about 2.5 meters per second, whereby the rate is established in the largest diameter conduit of the machine being cleaned.
Also, the superior process of this invention is calculated to be about 100% to about 650%, and preferably, from about 300% to about 600% faster than the conventional process shown in FIG.
1
.
It is also noted herein that when unused solution is supplied to the machine targeted for cleaning, disinfecting or both, via the process of this invention, it is preferred that the unused solution be pumped into the machine, intermittently. This means that the solution is pumped into the machine from about two seconds to about two minutes, and preferably, from about five seconds to abut 1.5 minutes, and most preferably, from about ten seconds to about one minute, followed by a resting period (no pumping or flow of solution) from about two seconds to about two minutes, and preferably, from about five seconds to abut 1.5 minutes, and most preferably, from about ten seconds to about one minute. Such intermittent pumping of solution minimizes the mixing of solutions that may be recirculated, thereby making cleaning, disinfecting or both more efficient. Also, during the resting period it is preferred the machine being subjected to solution be drained.
The prophetic example which follows below is provided to further illustrate and facilitate an understanding of the present invention. Therefore, the example is not meant to be limiting and modifications which fall within the scope and spirit of the claims are intended to be within the scope and spirit of the present invention.
EXAMPLE
A carbonated beverage filling machine may be cleaned in the manner outlined in
FIGS. 4
a
and
4
b.
When calculating the time to clean such a machine, via the conventional process outlined in
FIG. 4
a
and via the process of this invention outlined in
FIG. 4
b,
the residence time (RT) of the solution supplied in the machine and the soil conditions of each component of the machine being cleaned must be considered. In the current prophetic example, we assumed soil conditions to be the same for each machine subjected to solution. For both machines (e.g., the machine that may be subjected to the process set out in
FIG. 4
a
and the machine being subjected to the process set out in
FIG. 4
b
) we assumed the following would be required:
Pre-rinse for a period of 3 residence times;
Wash for a period of 4 residence times; and
Post-rinse for a period of 3 residence times.
Table I below depicts the time it would take to clean a carbonated beverage machine via the conventional process set forth in
FIG. 4
a,
and Table II depicts the time it would take to clean the same carbonated beverage machine with the process of this invention. As may be seen from the numbers, the conventional process would take 105 minutes and the process of this invention would take 35 minutes (i.e., time to complete the slowest step). Leg, as used herein, is defined to mean portion.
TABLE I
|
|
Current configuration
|
1 RT
Total
|
Step
secs
RTs (secs)
Comment
|
|
Pre-rinse A
20
200
parts B, C, and D still need pre-rinse
|
Pre-rinse B
40
400
parts C, and D still need pre-rinse
|
Pre-rinse C
60
600
part D still needs pre-rinse
|
Pre-rinse D
90
900
complete system pre-rinsed
|
Wash A
20
200
parts B, C, and D still dirty
|
Wash B
40
400
parts C, and D still dirty
|
Wash C
60
600
part D still dirty
|
Wash D
90
900
complete system pre-rinsed and washed
|
Post-rinse A
20
200
parts B, C, and D still need post-rinse
|
Post-rinse B
40
400
parts C, and D still needs post-rinse
|
Post-rinse C
60
600
part D still needs post-rinse
|
Post-rinse D
90
900
complete system pre-rinsed, washed,
|
and post-rinsed
|
total time required:
6300
seconds
|
105
minutes
|
|
TABLE I
|
|
Current configuration
|
1 RT
Total
|
Step
secs
RTs (secs)
Comment
|
|
Pre-rinse A
20
200
parts B, C, and D still need pre-rinse
|
Pre-rinse B
40
400
parts C, and D still need pre-rinse
|
Pre-rinse C
60
600
part D still needs pre-rinse
|
Pre-rinse D
90
900
complete system pre-rinsed
|
Wash A
20
200
parts B, C, and D still dirty
|
Wash B
40
400
parts C, and D still dirty
|
Wash C
60
600
part D still dirty
|
Wash D
90
900
complete system pre-rinsed and washed
|
Post-rinse A
20
200
parts B, C, and D still need post-rinse
|
Post-rinse B
40
400
parts C, and D still needs post-rinse
|
Post-rinse C
60
600
part D still needs post-rinse
|
Post-rinse D
90
900
complete system pre-rinsed, washed,
|
and post-rinsed
|
total time required:
6300
seconds
|
105
minutes
|
|
Claims
- 1. A cleaning-in-place process comprising the steps of:a) supplying an unused solution to more than two components of a machine targeted for cleaning, disinfecting or both; b) generating spent solution, and c) removing said spent solution through at least one outlet of the machine, wherein the unused solution is not supplied to a part of the machine that is only subjected to water and holds more than 5.0% of total volume of solution in the machine, and no more than 5.0% of the spent solution generated during the CIP process is mixed within the machine prior to exiting the machine.
- 2. The cleaning-in-place process according to claim 1 wherein the solution is a cleaning, sanitizing, rinsing or sanitizing and cleaning solution.
- 3. The cleaning-in-place process according to claim 2 wherein the solution is a cleaning solution and the cleaning solution comprises phosphoric acid or an enzyme.
- 4. The cleaning-in-place process according to claim 2 wherein the solution is a disinfecting solution and the disinfecting solution comprises an organochlorine donor, iodine donor, phosphoric acid, dodecylbenzene sulphonic acid or peroxyacetic acid.
- 5. The cleaning-in-place process according to claim 2 wherein the solution is a rinsing solution and the rinsing solution comprises a low foaming surfactant.
- 6. The cleaning-in-place process according to claim 1 wherein the machine is a carbonated beverage filling machine.
- 7. The cleaning-in-place process according to claim 6 wherein unused solution is supplied into at least three components of the machine.
- 8. The cleaning-in-place process according to claim 7 wherein the three components are a syrup recovery tank, a filler and a syrup bowl or water bowl.
- 9. The cleaning-in-place process according to claim 6 wherein the unused solution is supplied into four components.
- 10. The cleaning-in-place process according to claim 9 wherein the four components are a syrup recovery tank, a filler, a syrup bowl and a water bowl.
- 11. The cleaning-in-place process according to claim 6 wherein the process comprises two CIP units to supply unused solution to the machine.
- 12. The cleaning-in-place process according to claim 11 wherein one of the two CIP units supplies unused solution only to a syrup recovery tank.
- 13. The cleaning-in-place process according to claim 1 wherein the process further comprises the step of supplying the unused solution into the machine intermittently.
- 14. The cleaning-in-place process according to claim 13 wherein the solution is intermittently supplied to the machine by pumping solution for about two seconds to about two minutes followed by a resting period for about two seconds to about two minutes.
- 15. The cleaning-in-place process according to claim 1 wherein the process utilizes one CIP unit to supply unused solution to the machine.
- 16. The cleaning-in-place process according to claim 1 wherein the unused solution comprises a halogen dioxide.
- 17. The cleaning-in-place process according to claim 16 wherein the halogen dioxide is chlorine dioxide.
- 18. A machine having been washed by a cleaning-in-place process, said process comprising the steps of:a) supplying an unused solution to more than two components of the machine; b) generating spent solution; and c) removing said spent solution through at least one outlet of the machine wherein the unused solution is not supplied to a part of the machine that is only subjected to water and holds more than 5.0% of total volume of solution in the machine, and no more than 5.0% of the spent solution generated during the CIP process is mixed within the machine prior to exiting the machine.
- 19. The machine according to claim 18 wherein the machine is a non-fermentative carbonated beverage filling machine.
US Referenced Citations (7)