The object of the invention is an apparatus, as defined in the preamble of claim 1, for measuring the dewatering of a paper machine at different points of the wet end. In the invention, the water 7 removed from a roll 6 of the apparatus by means of centrifugal force or blowing is collected most preferably in a trough 3, or corresponding water receptacle, and is conducted by gravity along an inlet pipe 10 to a measuring system for measuring the dewatering at the wet end of the paper machine. The invention also relates to a method according to claim 11.
It is generally known in the art that when manufacturing paper, chemical pulp and board, different techniques for removing water from the fiber/water mixture, i.e. from the web, are used at the wet end of the machine. Water is separated from the web by means of centrifugal forces, negative pressure and/or wet pressing. The terms ‘paper web’ and ‘paper machine’ used hereinafter refer to all the aforementioned products and productions. It is important to measure the water separated from the web in different parts of the machine in order to optimize production efficiency. It is also worth measuring the water removed from the fabrics used in the press section for optimizing the machine and for fabric development.
Dewatering of the Web
One typical solution according to the state of the art, which is disclosed in specification U.S. Pat. No. 6,053,039, is the dewatering principle presented in
Measurement of Dewatering
Currently, magnetic flow meters are used to measure the flow rate of the water removed with the water drainage technique presented above. One problem, however, is that the drainage waters of a paper machine contain a lot of air. For this reason, with liquids containing air all the devices measuring the flow velocity of the liquid give a false result, as also does a magnetic flow meter, because the air content increases the flow velocity. Therefore, a second technique is used, i.e. weir flow measurement, that functions better with liquids containing air. Conventional weir flow measurement uses a V-orifice weir, the height of the surface formed by the weir being measured either with a pressure transmitter or with a surface height meter. In all measurements functioning on the weir principle, it is important that the flow velocity before the weir is controlled. In V-orifice measurements, a relatively long and straight pipe is needed before the measurement. A problem with a V-weir in a paper machine is the space requirement and the solids in the flows that easily lodge in the sharp bottom corner of the weir.
Another solution known from specifications U.S. Pat. No. 5,875,675 and US6053 is the weir plate 8 according to
Drawbacks and Problems of Prior Art
The measuring principles described above are widely used nowadays in the paper industry. However, they have some essential problems. Firstly, conducting water from above downwards for measuring requires a lot of space in the height direction. According to the state of the art, the meter must often be installed down in a basement in flow measurement of a trough. Piping costs increase, but the most detrimental issue from the viewpoint of the system is the high flow velocity of the water falling downwards, which distorts the measurement result. In addition to the high flow velocity, the high air content brought along with the water falling downwards also distorts the measurement result. The detrimental noise produced by falling water is also a problem.
The solution according to the invention is characterized by what is disclosed in the claims.
In the following a new system for measuring the drainage waters of a paper machine will be disclosed, which system resolves the problems known in the art and presented above.
According to the invention, a solution has been achieved wherein a new type of apparatus with which a method for measuring dewatering at the wet end of a paper machine can be utilized more efficiently both in dewatering points subject to atmospheric pressure and in dewatering points subject to negative pressure.
In the following, the invention will be described in more detail with reference to the attached drawings, wherein:
In the measuring system 26 according to the invention, the water 7 removed from the surface of a roll 6 is collected in a trough 3 and conducted along an inlet pipe 10 into the bottom part of the measuring receptacle 27 of the measuring system. The removal of air is implemented in the measuring system 26 with an expansion made in the inlet pipe 10, most preferably with an eccentric pipe reducer 14, which expands the internal volume of the pipe for separating air 22 from the water 7. The air 22 traveling along with the flow of the removed water 7 is in this way separated into the top part of the expanded pipe 15 and is guided onwards into an outlet pipe 16 that is open at the top. Most of the air 22 discharges along the pipe 16 and the rest of the remaining air 22 is separated along with the flow in the deaeration chamber 17. The removed water 7 flows from the deaeration chamber 17 via a water seal 21 into the measuring chamber 18, in which is most preferably the A-shaped 9 weir plate according to
According to what is presented above, what is essential in the invention is that the measuring chamber 18, the deaeration chamber 17, together with the inlet pipe 10 and the pipe section 15 expanded with a pipe reducer 14 formed in it for deaerating, as well as with the outlet pipe 16 open at the top, form receptacles uniting integrally with each other. In this way, the large water capacity important to the measuring system 26 according to the invention is achieved, the capacity allowing a calm, controlled and air-free flow to the measuring weir 8.
In the invention, a pressure transmitter 20 measures the height of the water level produced by the measuring weir 8. A transmitter 20 that is provided with e.g. a 50 mm membrane is used in the solution. What is essential is that the membrane of the transmitter does not clog with dirt, such as e.g. a thin pressure transmission pipe according to what is known in the art. In addition, the transmitter 20 is situated in such a way that the center line of the membrane is level with the bottom surface of the weir 8. The size of the measuring receptacle 27 functioning as a meter of the measuring system 26 depends on the flow rates; for example, the height*width*depth for a maximum flow of 1000 l/min are 0.6*0.7*0.5 m.
The solution according to the invention saves space in the height direction because the removed water 7 is guided along the inlet pipe 10 through the pipe section 15 expanded with a pipe reducer 14 and through the D-shaped orifice 23 into the essentially horizontal bottom part of the deaeration chamber 17. The outlet pipe 19 leaving from the measuring chamber 18 of the measuring system 26 is oriented either downwards or horizontally, depending on the space in which the measuring chamber 18 is installed. This property reduces the height space required to the minimum; that being the case, the whole measuring system 26 can be installed on the machine level 11.
It is obvious, according to what is presented above, that considerable advantages are gained with the invention. The solution according to the invention is considerably more compact and less expensive to manufacture than a solution describing the state of the art, and also the measurement result is better.
What is essential in the measuring system is that it comprises:
It is obvious to the person skilled in the art that the invention is not limited to the embodiments presented above, but that it can be varied within the scope of the claims presented below, which form a method and an apparatus for the measuring system 26 according to the invention.
Number | Date | Country | Kind |
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20175092 | Feb 2017 | FI | national |
Filing Document | Filing Date | Country | Kind |
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PCT/FI2018/050020 | 1/11/2018 | WO | 00 |