This application is the United States national phase of International Application No. PCT/EP2014/069584 filed Sep. 15, 2014, and claims priority to German Application No. 10 2013 219 464.1 filed Sep. 26, 2013, the disclosures of which are hereby incorporated in their entirety by reference.
The invention relates to a device and a method for evacuating a film chamber.
Film chambers are made of a flexible, soft material—mostly films—and are used in detecting leaks in packages. A specimen to be examined for a leak is placed in the film chamber. Most often, the specimen is a food package also made of a flexible material. The film chamber surrounding the specimen is evacuated. Thereafter, the pressure or the gas in the film chamber is monitored so as to test the tightness of the specimen and to detect a possible leak in the specimen.
Conventional film chambers are evacuated using vacuum pumps having a high suction capacity and achieving a low end pressure. Such pumps are heavy and require high electric power for operation.
Smaller, lighter pumps either have a high suction capacity or can reach a low pressure so that they are not suited as the single replacement of conventional pumps.
It is an object of the invention to provide an evacuation device, as well as a corresponding method for evacuating a film chamber so as to reach a high suction capacity and a low end pressure with smaller pumps.
A film chamber is evacuated by a pump system having at least two vacuum pumps connected in parallel and each connected with the film chamber. The two vacuum pumps are designed for an alternating evacuation of the film chamber, i.e. they are operated alternately or are alternately connected with the film chamber. As an alternative it is conceivable that the two vacuum pumps are connected with the film chamber by a common pipeline, the two vacuum pumps being alternately connected with the common pipeline by a valve or a switch element.
The suction capacity of the first vacuum pump is higher than that of the second vacuum pump, with the end pressure achievable by the second vacuum pump being lower than that of the first vacuum pump. Thus, both vacuum pumps are, each individually, lighter than the conventionally used heavy vacuum pumps. Whereas, conventionally, one large vacuum pump was used that can reach both the desired end pressure and the required suction capacity, a device according to the present invention can be based on the idea to use one vacuum pump for the desired suction capacity and one for the end pressure to be reached. These two vacuum pumps are operated alternately one after the other. Here, the vacuum pump having the higher suction capacity is used first for a rough evacuation of the film chamber. The other vacuum pump that can reach the lower end pressure is used thereafter to reach the end pressure.
In this regard it is advantageous to provide a buffer chamber between the second vacuum pump and the film chamber, the buffer chamber being evacuated by the second vacuum pump, while the first vacuum pump evacuates the film chamber. Thus, when the second vacuum pump is not connected with the film chamber, it evacuates the buffer chamber and, in doing so, preferably already reaches the end pressure desired in the film chamber. Thereafter, the film chamber is evacuated by the buffer chamber and possibly also by the second vacuum pump. Thereby, it is possible to significantly reduce the time in which the film chamber is brought to the desired end pressure.
The suction capacity of the first vacuum pump is preferably higher than the initial volume of the film chamber in liters per second (l/s, e.g. more than 1 l/s for an initial volume of 1 l) and its end pressure is higher than 50 millibars (mbar). Preferably, the suction capacity of the second vacuum pump is less than the pre-evacuated residual volume of the film chamber in l/s (e.g. less than 0.25 l/s for 250 cm3) and its end pressure is less than 50 mbar. Such vacuum pumps are each sufficiently light and adapted for mobile use and, in the combination according to the invention, may still be sufficiently fast in evacuating a film chamber to the required end pressure.
The first vacuum pump may be at least one jet pump, e.g. a Venturi pump. In this regard it is conceivable that it is either exactly one jet pump or a plurality of jet pumps connected in series one behind the other.
The buffer chamber between the second port and the second vacuum pump should preferably have an evacuable volume in the range between six and eight times the volume of the film chamber volume and preferably in the range between nine and eleven tines the film chamber volume.
In a variant in which the two vacuum pumps are connected with the film chamber by a common pipeline, a valve with at least three ports may be provided in order to connect the two vacuum pumps and the pipe line or the film chamber.
The valve may preferably be a 3/2-way valve. The first port of the valve is connected with a first vacuum pump. The second port is connected with a second vacuum pump. The third port serves to connect the film chamber. The valve has at least two switching positions. In the first switching position the valve connects the first port and the third port with each other, i.e. the first vacuum pump and the film chamber. In the second switching position the valve connects the second and the third port with each other, i.e. the second vacuum pump and the film chamber. There is no switching position in which the first and the second port of the valve are connected with each other. The first vacuum pump is thus never connected with the second vacuum pump. Rather, the two vacuum pumps are alternately connected with the film chamber so as to evacuate the same one after the other.
A method for evacuating a film chamber includes evacuating the film chamber by the first vacuum pump having the higher suction capacity. For this purpose, the first vacuum pump may be connected with the film chamber and the second vacuum pump may be separated from the film chamber. Thereafter, the second vacuum pump is used to reach the low end pressure in the film chamber. To this end, the first vacuum pump may be separated from the film chamber and the second vacuum pump may be connected with the film chamber. In this regard it is advantageous if, prior to connecting the second vacuum pump with the film chamber, a buffer chamber is evacuated by the second vacuum pump. In the meantime, for example, the film chamber may already be evacuated by the first vacuum pump with the higher suction capacity.
A central core element of a device according to the example embodiments is a 3/2-way valve 12 having three ports 14, 16, 18 and two operating paths. A first vacuum pump 20 in the form of a Venturi pump is connected with the first port 14. A second vacuum pump 22 in form of a displacement pump is connected with the second port 16. The pipeline 24 connecting the second port 16 with the second vacuum pump 22 is connected with a buffer chamber 26 in a gas-conveying manner. The third port 18 is connected with the film chamber 28 via a pipeline 25. A stop valve 30 is arranged in the pipeline 25 between the film chamber 28 and the third port 18. As an alternative, it is conceivable that each of the two vacuum pumps 20, 22 is connected with the film chamber 28 via an own separate pipeline.
The film chamber 28 includes or consists of two film layers 32, 34 between which the specimen 36 is arranged.
The Venturi pump 20 is connected with a valve 38 so as to be able to control the operation of the pump 20.
The device can be based on the idea to combine a pump having a high suction capacity, but also a high end pressure, with a pump having a low end pressure, but a low suction capacity. These two pumps 20, 22 are selectively and alternately connected with the film chamber 28 via the 3/2-way valve 12 so as to evacuate the film chamber.
At the beginning, as illustrated in
As shown in
Thereafter, as illustrated in
In order to bring the film chamber 28 to the desired end pressure to be reached, the operational state of the device of the present invention as illustrated in
While the first vacuum pump 20 (Venturi pump) can only reach an end pressure of 200 mbar, the second vacuum pump 22 can reach an end pressure of only 20 mbar. During the second operational state illustrated in
p=(200 mbar·50 cm3+20 mbar·500 cm3)/(550 cm3)=36 mbar.
Number | Date | Country | Kind |
---|---|---|---|
10 2013 219 464 | Sep 2013 | DE | national |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2014/069584 | 9/15/2014 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2015/043993 | 4/2/2015 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
4791806 | Wade | Dec 1988 | A |
4984450 | Burger | Jan 1991 | A |
5107697 | Tallon | Apr 1992 | A |
5131263 | Handke | Jul 1992 | A |
6004109 | Gebele | Dec 1999 | A |
6354142 | Nothhelfer et al. | Mar 2002 | B1 |
6446651 | Abbel | Sep 2002 | B1 |
6945092 | Widt | Sep 2005 | B2 |
6955076 | Widt | Oct 2005 | B1 |
7914265 | Coles | Mar 2011 | B2 |
20030068233 | Royce | Apr 2003 | A1 |
20030233866 | Widt | Dec 2003 | A1 |
20090208649 | Bailey | Aug 2009 | A1 |
20110126936 | Dawson | Jun 2011 | A1 |
20120255445 | Haruna | Oct 2012 | A1 |
20130259712 | Kawasaki | Oct 2013 | A1 |
20140311222 | Decker et al. | Oct 2014 | A1 |
Number | Date | Country |
---|---|---|
82183 | May 1971 | DE |
96304 | Mar 1973 | DE |
3639512 | Jun 1988 | DE |
102005042451 | Mar 2007 | DE |
102012200063 | Jul 2013 | DE |
0752531 | Jan 1997 | EP |
6024057 | Feb 1985 | JP |
7325279 | Dec 1995 | JP |
9196797 | Jul 1997 | JP |
2001508536 | Jun 2001 | JP |
0146667 | Jun 2001 | WO |
2013072173 | May 2013 | WO |
Number | Date | Country | |
---|---|---|---|
20160258448 A1 | Sep 2016 | US |