Patent Application
20150360149
The invention relates to a method for air drying a filter cake contained in a filter chamber defined by a first filter plate, which comprises an air inlet for supplying drying air into the filter chamber to expel fluids from the filter cake, and a second filter plate, which comprises a fluid outlet for discharging fluids from the filter chamber.
The invention also relates to a filter plate for a filter press, comprising a recess for defining a filter chamber in co-operation with a corresponding recess of a contiguous filter plate and an air inlet for supplying drying air into the recess for air drying a filter cake contained in the filter chamber.
Filter plates are used in filter presses for dewatering suspensions or slurries. In a filter press, a row of filter plates forms a solid plate pack of sealed filter chambers with two filter cloths in between each pair of plates. Process fluids are supplied to each filter chamber via one or more inlet channels and filtrate is discharged from each filter chamber via one or more outlet channels.
When starting a filtration cycle, the filter plates are first pressed tight against each other to seal the filter chambers. During a filling step, slurry to be dewatered is pumped via a slurry inlet channel into all filter chambers simultaneously. During a filtration step, solids are captured by the filter cloth to form a filter cake. At the same time, liquid penetrates through the filter cloth and the filtrate is drained from the filter chamber via one or more drainage outlets. A filter plate of a pressure filter can comprise an inflatable membrane. During a squeezing step, the membrane is inflated by pressurized medium, such as compressed air or pressurized water, to impose mechanical compression via the membrane on the filter cake, thus reducing the moisture content of the cake. During a washing step the filter cake is washed by impelling washing liquid to the cake and discharging the washing filtrate. During a drying step, compressed air is forced through the filter cake to achieve low residual moisture content before the filter cake is finally removed from the filter chamber.
The drying air is under pressure when it is fed into the filter chamber, where it pushes residual liquid through the filter cake. In the filter chamber, the pressure of the drying air reduces and the air expands.
Current filter plate packs are bearing the risk of unequal chamber conditions after the filtration step. The unequal conditions include inadequate thickness of the filter cake, uneven cake distribution in a single filter chamber, or uneven cake distribution over the plate pack length. This results in differences in air flow in individual chambers during the air drying step. Some chambers can take very high air flows because of total or partial short cuts. High air flow through a filter chamber causes a high risk of filter plate erosion and other damages.
The purpose of the invention is to eliminate the problems of prior art and to improve the reliability of filter cake air drying system.
One purpose is to eliminate the risk of damages caused by exceptional conditions in a filter chamber during the air drying of a filter cake.
Another purpose is to equalize the air flow into different filter chambers in a plate pack during the air drying of filter cakes.
The invention is characterized by what is presented in independent claims 1 and 5.
The invention relates to a method for air drying a filter cake contained in a filter chamber defined by a first filter plate, which comprises an air inlet for supplying drying air into the filter chamber to expel fluids from the filter cake, and a second filter plate, which comprises a fluid outlet for discharging fluids from the filter chamber. The method comprises throttling the air flow into the filter chamber by means of a flow regulating device contained in the first filter plate, which flow regulating device acts as a flow resistance connected in series with the flow resistance of the filter chamber.
According to one aspect of the invention, the flow regulating device is selected from a group comprising an orifice plate, an adjustable orifice plate, a throttle valve, and an adjustable valve.
According to another aspect of the invention, the orifice of the orifice plate is so sized that, in case the flow resistance of the filter chamber falls below a normal level, choked flow is achieved in the orifice.
According to another aspect of the invention, a fluid outlet contained in the first filter plate is blocked during the air drying. In that way the filter chamber is isolated from other filter chambers.
The invention also relates to a filter plate that comprises a recess for defining a filter chamber in co-operation with a corresponding recess in a contiguous filter plate and an air inlet for supplying drying air into the recess for air drying a filter cake contained in the filter chamber. The filter plate comprises a regulating device for regulating the air flow from the air inlet into the filter chamber, which regulating device acts as a flow resistance connected in series with the flow resistance of the filter chamber.
According to one aspect of the invention, the flow regulating device is selected from a group comprising an orifice plate, an adjustable orifice plate, a throttle valve, and an adjustable valve.
According to another aspect of the invention, the filter plate comprises at least one fluid outlet for discharging fluids from the filter chamber and a valve for blocking the fluid outlet during air drying of the filter cake.
According to one aspect of the invention, the orifice of the orifice plate is so sized that choked flow is achieved when the flow resistance of the filter chamber falls below a normal level. Also the cross-sectional area of the fluid outlet in the contiguous filter plate can be taken into account when sizing the orifice in the orifice plate. The dimensioning of the orifice can be done in such a way that even with none or just a minimal chamber pressure loss the total air flow is restricted to an acceptable value.
When the pressure upstream of the orifice plate is constant and the pressure downstream is gradually reduced, the pressure difference across the orifice plate grows, increasing both the gas velocity and the gas flow through the restriction. Eventually, as the downstream pressure is dropped further, the flow through the orifice plate becomes sonic. This is often referred to as choked flow, and it is a physical limit. Any further drop in the downstream pressure will not result in increase of gas flow. Once the flow becomes choked, it is independent of conditions downstream of the restriction.
Choked flow is useful in drying filter cakes in a filter press because the mass flow rate is independent of the downstream pressure, depending only on the temperature and pressure on the upstream side of the restriction. Under choked conditions, calibrated orifice plates can be used to produce a desired mass flow rate.
The accompanying drawings, which are included to provide a further understanding of the invention and constitute a part of this specification, illustrate embodiments of the invention and together with the description help to explain the principles of the invention. In the drawings:
A plate pack used in a filter press can be a mixed pack consisting of alternating membrane filter plates and chamber filter plates, or it can be a combi pack consisting of so called combi filter plates. The following description is based on a mixed pack construction, but the invention can as well be used in connection with combi filter plates, where the same filter plate comprises a membrane filter plate side and a chamber filter plate side.
The orifice plate 13, which is shown in more detail in
The block valve 10 can be of any suitable type. One example of a possible block valve 10 is shown in detail in
During the operation of a filter press, a membrane filter plate 2 and a chamber filter plate 14 are pressed together so that a filter chamber is defined by the recess 4 of the membrane filter plate 2 and the recess 15 of the chamber filter plate 14. The bottom of each recess 4, 15 is corrugated in one way or another. Two filter cloths are placed into the filter chamber and the slurry to be filtrated is fed in between the filter cloths via a feed shoe so that the slurry forces the filter clothes against the corrugated surfaces of the recesses 4, 15. These corrugated surfaces collect the filtrate permeating through the filter cloths. The solids of the slurry are retained between the filter cloths, forming a filter cake. The filtrate collected in the corrugated surfaces of the recesses 4, 15 is discharged via the first fluid outlet 7 in the membrane filter plate 2 and via the second fluid outlet 18 in the chamber filter plate 14.
To dry the filter cake contained in a filter chamber, pressurized air is fed via an air inlet 9, orifice plate 13, first fluid duct 6 and fluid conduits 8 to the recess 4 in the first filter plate 2. The drying air penetrates through the filter cake. The mixture of air and filtrate expelled from the filter cake is drained via the bore holes 17, second fluid duct 12 and second outlet 18 of the second filter plate 14. The orifice plate 13 acts as a flow resistance connected in series with the flow resistance of the filter chamber, throttling the air flow into the filter chamber.
The principle of air drying with air throttling arranged in connection with each filter chamber will now be described with a view to
The system may also comprise an optional water source 27 that can be connected to the air supply line 22 during the slurry feeding and cake squeezing steps. During these steps, small amounts of water can be fed via each air inlet 9 into each recess 4 to prevent contamination or blocking of the orifice plate 13 by the filtrate contained in the recess 4.
An explanation of the symbols to be used in the following description is given below:
The air pressure p0 in the air supply line 22 is selected based on the application and filter type in question. The drying air pressure pi in each chamber 19 is chamber specific. The chamber specific drying air pressure pi depends on the permeability of the filter cake and filter cloths, the area AOR of the orifice 21 in the orifice plate 13, the absolute pressure p0 in the air supply line 22, the back pressure pSF in the second filtrate collector 24, the area AEX of the second fluid outlet 18, and the absolute temperature T0 of the drying air feed. The area AOR of the orifice 21 is preferably similar in each plate 2. The permeability of the filter cake and filter clothes influence the flow resistance of the filter chamber 19.
During an ideal operation of the air drying system, the chamber specific drying air pressure pi is identical in each filter chamber 19. Also the air mass flow {dot over (m)}i into each filter chamber 19 is essentially the same. Occasionally, the flow resistance in one of the filter chambers can be different from the flow resistances in the other filter chambers in the filter pack. This results in a different drying air pressure piOUT in the filter chamber in question.
Dimensioning of the cross-sectional area AOR of the orifice 21 is based on the fact that the flow velocity viIN should be the same in each filter chamber 19 and that the flow speed viOUT should always be smaller than the maximum flow velocity vCRIT in which erosion does not occur. If the flow velocity viOUT in a filter chamber is higher than the critical velocity vCRIT, there is a high risk of erosion in the parts 16, 17, 18 of the second filter plate 14 which get into contact with the increased air flow.
The idea of the present invention is to produce a choked flow phenomenon in a filter chamber in which the flow resistance is reduced for one reason or another. Such unusual conditions in a filter chamber include, for instance, broken filter cloths, missing, thin or uneven filter cake, etc. In the healthy chambers the chamber specific drying air pressures piOUT are essentially identical, and the chamber specific mass flow {dot over (m)}i through each orifice plate 13 is essentially the same in each healthy chamber.
However, in a filter chamber with odd conditions, the chamber specific drying air pressure piOUT is much the same as the back pressure pSF in the chamber side filtrate collector 24. The flow speed viIN in the orifice plate 13 of the “sick” filter chamber is higher than the flow speed in the orifice plates of “healthy” filter chambers.
Choked flow occurs when the gas velocity across a restriction in a flow path becomes sonic. This is a maximum velocity which limits the gas flow. An orifice plate 13 is simply a plate with a hole 21 in it to restrict the air flow, resulting in a pressure drop. When the pressure downstream of the orifice plate is low enough, the air flow through the orifice plate 13 becomes sonic. This is often referred to as choked flow and it is a physical limit. Any further drop in the downstream pressure will not result in an increase in gas flow. Once the flow becomes choked, it is independent of conditions downstream of the restriction.
As there is a choked flow phenomenon in a sick filter chamber, flow speed viIN in the orifice plate 13 of the filter chamber is essentially the same as the sonic speed, but it does not rise further. Having carefully determined the ratio of the area AEX of the fluid outlet opening 18 to the area AOR of the orifice 21, we still have a velocity viOUT which is below the critical velocity VCRIT. At the same time, the air mass flow {dot over (m)}i in healthy filter chambers is maintained on an effective level.
Fore-throttling is used to restrict the mass flow {dot over (m)}i of drying air by means of choked flow phenomenon to such a threshold below which the velocity viOUT of the exiting air, which has expanded due to the pressure drop, does not cause serious erosion together with solid particles.
Throttling of drying air supply is feasible only when the filter chambers 19 can be kept separate from each other so that there is no pressure equalization route between individual filter chambers. In addition to the previously mentioned block valves 10 between the firs recess 4 and the first drainage line 25, also filling shoes (not shown) or membranes can act as blocking elements that block the pressure equalization routes between individual filter chambers 19.
An orifice plate 13 installed in connection with an air supply inlet 9 acts as a serial flow resistance to the chamber flow resistance. As long as the chamber flow resistance is within a normal level, the flow resistance of the orifice 21 is adding up only a relatively small pressure loss to the overall resistance chain. In case the flow resistance in one or more chambers 19 reduces below a specified value, the air mass flow mi increases and the pressure loss over the orifice 21 increases correspondingly, resulting in a choked flow.
The invention allows remarkable increase in the operational safety of filter press operations.
A conventional solution would comprise controlling only the total air mass flow {dot over (m)}TOT from the air source 21 to the filter chambers 19 by means of a control valve, pressure transmitter, pressure reducer, orifice plate, etc. This kind of solution does not allow attending to disturbances in individual filter chambers. A filter plate pack may contain tens of filter chambers, in which case the eroding oversized air mass flow {dot over (m)}i into one filter chamber does not affect significantly the total air mass flow {dot over (m)}TOT.
It is obvious to a person skilled in the art that with the advancement of technology, the basic idea of the invention may be implemented in various ways. The invention and its embodiments are thus not limited to the examples described above; instead they may vary within the scope of the claims. For instance, the orifice plate described above may be replaced with an adjustable orifice plate, a throttle valve, an adjustable valve, or any other suitable type of regulating device for regulating the air flow from the air inlet into the flow chamber.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20135149 | Feb 2013 | FI | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/FI2014/050120 | 2/18/2014 | WO | 00 |
