A SYSTEM FOR TRANSPORTING BIOMASS MATERIAL AND A METHOD FOR PREVENTING BLOW BACK IN SAID SYSTEM
20210039893 · 2021-02-11
Assignee
Inventors
Cpc classification
B30B9/3096
PERFORMING OPERATIONS; TRANSPORTING
B65G33/22
PERFORMING OPERATIONS; TRANSPORTING
International classification
B65G43/02
PERFORMING OPERATIONS; TRANSPORTING
B30B9/12
PERFORMING OPERATIONS; TRANSPORTING
B65G33/22
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention relates to a system (1) comprising a feeding device (2) comprising a channel (6) having an inlet (8) and an outlet (10) and a feed screw (12) for conveying biomass material through the channel. The feed screw comprises a screw flight (12b) that extends from a first end (12c) to a second end (12d) and is adapted to form a gas impermeable plug of biomass. The system comprises at least one primary measuring unit (14; 16) adapted to continuously measure a primary variable indicative of the gas permeability of the plug, which primary measuring unit is connected to said feeding device between the first end of the screw flight and the outlet; and a control unit (3) adapted to use said primary variable values to monitor the gas permeability of the plug. The invention also relates to a method for preventing blow back in the above described system.
Claims
1. A system for transporting biomass material, which system comprises a feeding device comprising: a channel comprising an inlet and an outlet for said biomass material; and a feed screw arranged at least partly within the channel and comprising a screw flight for conveying the biomass material in a biomass transport direction from the inlet to the outlet, which screw flight is also adapted to compress the biomass material during transport to form a gas impermeable plug of biomass material within the channel, and which screw flight extends from a first end to a second end in the biomass transport direction; characterized in that said system further comprises: at least one primary measuring unit adapted to continuously measure a primary variable indicative of the gas permeability of the plug, which primary measuring unit is connected to said feeding device between the first end of the screw flight and the outlet; and a control unit adapted to continuously receive primary variable values from the primary measuring unit and use said primary variable values to monitor the gas permeability of the plug.
2. A system according to claim 1, which system comprises a primary measuring unit adapted to measure a force and/or pressure exerted by the plug.
3. A system according to claim 1, which system comprises a primary measuring unit adapted to measure a temperature within the channel.
4. A system according to claim 1, wherein said control unit is adapted to provide a warning signal when the gas permeability of the plug is above an upper gas permeability threshold.
5. A system according to claim 4, wherein said control unit is adapted to automatically control at least one density regulating means to increase the density of the plug when the gas permeability of the plug is above the upper gas permeability threshold.
6. A system according to claim 1, wherein said primary variable is indicative of the radial pressure exerted by the plug and the control unit is adapted to use said primary variable values to monitor the radial pressure exerted by the plug.
7. A system according to claim 6, wherein said control unit is adapted to provide a warning signal when the radial pressure is above an upper radial pressure threshold.
8. A system according to claim 7, wherein said control unit is adapted to automatically control at least one density regulating means to reduce the density of the plug when the radial pressure of the plug exceeds the upper radial pressure threshold.
9. A system according to claim 1, wherein said primary measuring unit is arranged within a distance from the second end of the screw flight, which distance is 10 times the diameter of the channel at said second end, preferably 5 times the diameter of the channel at said second end, and even more preferably 1 times the diameter of the channel at said second end.
10. A system according to claim 4, which system comprises a gas pressure measuring unit arranged to continuously measure the gas pressure within a pressurized zone connected to the outlet, and wherein said control unit is adapted to continuously receive gas pressure values from the gas measuring unit and use said gas pressure values to determine the upper gas permeability threshold.
11. A method for preventing blow back in a system for transporting biomass material, which system comprises a feeding device comprising: a channel comprising an inlet and an outlet for said biomass material; and a feed screw arranged at least partly within the channel and comprising a screw flight for conveying the biomass material in a biomass transport direction from the inlet to the outlet, which screw flight is also adapted to compress the biomass material during transport to form a gas impermeable plug of biomass material within the channel, and which screw flight extends from a first end to a second end in the biomass transport direction; which method is characterized in that it comprises the steps of: at least one primary measuring unit connected to said feeding device between the first end of the screw flight and the outlet continuously measuring a primary variable indicative of the gas permeability of the plug; said primary measuring unit continuously transmitting primary variable values to a control unit; and said control unit using said primary values to monitor the gas permeability of the plug.
12. Method according to claim 11, which method comprises the step of a primary measuring unit measuring a force and/or pressure exerted by the plug.
13. Method according to claim 11, which method comprises the step of a primary measuring unit measuring a temperature within the channel.
14. A method according to claim 11, which method comprises the step of said control unit providing a warning signal when the gas permeability of the plug is above an upper gas permeability threshold.
15. A method according to claim 14, which method comprises the step of said control unit automatically controlling at least one density regulating means to increase the density of the plug when the gas permeability of the plug is above the upper gas permeability threshold.
16. A method according to claim 11, wherein the primary variable is indicative of the radial pressure exerted by the plug, which method comprises the step of said control unit using said primary variable values to monitor the radial pressure exerted by the plug.
17. A method according to claim 16, which method comprises the step of said control unit providing a warning signal when the radial pressure is above an upper radial pressure threshold.
18. A method according to claim 17, which method comprises the step of said control unit automatically controlling at least one density regulating means to reduce the density of plug when the radial pressure of the plug exceeds the upper radial pressure threshold.
19. A method according to claim 11, which method comprises the step of measuring said primary variable within a distance from the second end of the screw flight, which distance is 10 times the diameter of the channel at said second end, preferably 5 times the diameter of the channel at said second end, and even more preferably 1 times the diameter of the channel at said second end.
20. A method according to claim 14, which method comprises the steps of: a gas pressure measuring unit continuously measuring the gas pressure within a pressurized zone connected to the outlet; said gas pressure measuring unit continuously transmitting gas pressure values to the control unit; and said control unit using said gas pressure values to determine the upper gas permeability threshold.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0041] The present invention will be further explained hereinafter by means of non-limiting examples and with reference to the appended drawing, wherein:
[0042]
[0043]
DETAILED DESCRIPTION OF THE INVENTION
[0044] In the following description, like parts are referred to an indicated by like reference signs. Some parts have been removed from the figures for the sake of clarity.
[0045]
[0046] The feeding device 2 comprises a housing 4 that defines a channel 6 that extends along a longitudinal axis X of the feeding device 2. The channel 6 is divided into an inlet section 51, an intermediate section S2 and an outlet section S3. The inlet section 51 comprises an inlet 8 for biomass material and the outlet section S3 comprises an outlet 10 for biomass material. The inlet 8 is adapted to be connected to a feeding device (not shown) for feeding 25 biomass into the channel 6. Such a feeding device may, for example, comprise a force feed screw adapted to transport the biomass towards the inlet 8. The outlet 10 is adapted to be connected to a charger (not shown) to allow the biomass to be discharged from the channel 6 and into said charger.
[0047] A feed screw 12 extends into the housing 4 along the longitudinal axis X of the feeding device 2 towards the outlet 10. The feed screw 12 is adapted to convey the biomass material in a biomass transport direction from the inlet 8 to the outlet 10. The feed screw 12 comprises a central shaft 12a, which at one end is connected to and arranged to be rotated by a first drive mechanism M.sub.1. A screw flight 12b in the form of a screw helix (schematically shown) adapted to convey the biomass in the biomass transport direction extends around a portion of the central shaft 12a, from a first end 12c to a second end 12d, with a suitable pitch. The second end 12d is located at a distance from the outlet 10.
[0048] The biomass is compressed during transport through the channel 6, so that a gas impermeable plug of biomass is formed within the channel 6. Most of this compression occurs within the intermediate section S2, which has a narrowing cross-section towards the outlet 10, unlike the inlet and outlet sections S1 and S2, which have essentially constant cross-sections along the longitudinal axis X of the feeding device 2.
[0049] The biomass may be subjected to additional treatment during transport through the channel 6. The biomass may, for example, be subjected to dewatering, in which case additional pipes (not shown) may be connected to the channel 6 for transporting excess fluids away from the channel 6. Such means are known to the skilled person and will not be described in detail herein.
[0050] A primary measuring unit 14 in the form of a pressure sensor extends into the channel 6 at the second end 12d of the screw flight 12b. The pressure sensor is connected to the control unit 3. The pressure sensor is in this embodiment arranged to come into contact with the plug within the channel 6. The pressure sensor is adapted to measure a primary variable, in this embodiment the radial pressure (orthogonal to the longitudinal axis X of the feeding device 2) applied thereto. This radial pressure has two components, the pressure applied by the biomass that constitutes the plug and the pressure applied by the gas present within the pores of the plug. The pressure exerted by the gas is usually more or less negligible in comparison to the radial pressure exerted by the biomass. However, it is still advantageous to position the pressure sensor at the second end 12d of the screw flight 12b, because this is where the density of the plug is highest and thus also where the difference between the radial pressure applied by the biomass and the pressure applied by the gas is the largest. Thus, by positioning the pressure sensor at the second end 12d of the screw flight 12b is ensured that the radial pressure applied by the gas is negligible in comparison to the radial pressure applied by the biomass, and it can be assumed that the measured radial pressure is equal to the radial pressure exerted by the plug of biomass.
[0051] The measured radial pressure is indicative of the gas permeability of the plug, i.e. it can be used to determine the gas permeability of the plug. The control unit 3 compares the primary values, i.e. radial pressure values, received from the pressure sensor 14 to a lower radial pressure threshold corresponding to an upper gas permeability threshold to determine if the there is an increased risk of blow back. If the comparison shows that the radial pressure has dropped below the lower radial pressure threshold, then the control unit 3 sends out an alert (e.g. in the form of a light, sound or text message) to make an operator of the system aware that there is an increased risk of blow back. The operator may then, for example, reduce the rotational speed of the motor M.sub.1 to increase the density of the plug and make it essentially gas impermeable.
[0052] The control unit 3 may also be adapted to compare the primary values to an upper radial pressure threshold to determine if there is an increased risk of plugging of the channel 6. If the comparison reveals that the density of the plug is so high that there is an increased risk of plugging, then the control unit 3 sends out an alert to make the operator aware that there is an increased risk of plugging. The operator may then, for example, increase the rotational speed of the motor M.sub.1 to reduce the density of the plug and thus the risk of plugging.
[0053]
[0054] The system 1 also comprises a feeding device 24 for delivering biomass to the feeding device 2, which feeding device 24 comprises a feed screw 26 driven by a second drive mechanism M.sub.2.
[0055] The outlet 10 of the feeding device 2 is connected to a charger 20 arranged to receive biomass from the feeding device 2. A blow back damper 23 extends into the charger 20. The blow back damper 23 is arranged to be moved reciprocally towards and away from the outlet 10 of the feeding channel 6 by means of a hydraulic or pneumatic system S. The blow back damper 23 comprises a shaft 23a and a damper head 23b, which damper head 23b is moveable between a first position, in which it closes the outlet 10, and a second position, in which the damper head 23b is sufficiently far removed from the outlet 10 to ensure that the damper head 23b does not interact with the biomass being discharged through the outlet 10. The damper head 23b may occupy any position between the first and second positions, and is during use often positioned at a distance from the outlet 10 but still within reach of the biomass that is discharged through the outlet 10, so that the damper head 23b is used to shred the plug of biomass being discharged from the feeding device 2 while exerting a counter-pressure on said plug of biomass.
[0056] The biomass may be subjected to further treatment within the charger 20 and for this purpose, additional means (now shown), e.g. pipes, may be arranged within or connected to the charger. Such means are known to the skilled person and will not be described in detail herein.
[0057] The charger further comprises a charger outlet 28, through which biomass is conveyed to a pressurized reactor 21, wherein the biomass may be subjected to different types of treatments. A gas pressure measuring unit 22 in the form of a gas pressure sensor is arranged within the charger 21 and adapted to continuously measure the gas pressure within the charger 21 and send measured gas pressure values to the control unit 3.
[0058] The control unit 3 is connected to both the strain gauge and the gas pressure measuring unit 22, the hydraulic or pneumatic system S as well as to the first and second drive mechanisms M.sub.1 and M.sub.2, so that the control unit 3 may control the hydraulic or pneumatic system S and the first and second drive mechanisms M.sub.1, M.sub.2 in response to data received from the primary measuring unit 16 and the gas pressure measuring units 22.
[0059] The method for preventing blow back through the feeding device 2 will now be described in detail with reference to
[0060] The biomass is conveyed through the feeding device 24 by means of the feed screw 26 driven by the second drive mechanism M.sub.2. The biomass is delivered through the inlet 8 into the channel 6 within the feeding device 2. The first drive mechanism M.sub.1 rotates the feed screw 12 and the screw flight 12b extending along a portion of the feed screw 12 conveys the biomass in the biomass transport direction towards the outlet 10. During transport the biomass is compressed, partly due to the narrowing cross-section of the channel 6, and forms an essentially gas impermeable plug within the channel 6.
[0061] The blow back damper head 23b is initially positioned in the first position, wherein the damper head 23b closes the outlet 10. Thus, the damper head 23b prevents the biomass from entering the chamber and prevents gas from the pressurized reactor from 21 entering the feeding device 2. The damper head 23b applies a counter pressure to the biomass within the channel 6 and contributes to the formation of the gas impermeably plug.
[0062] The compressed biomass within the channel 6 exerts an increasing pressure on the damper head 23b and eventually pushes the damper head 23b in a direction away from the outlet 10, so that the plug of biomass may be discharged through the outlet 10 and into the charger 23, wherein it is shredded by the damper head 23b and the biomass falls towards the bottom of the charger 23. The counter pressure applied by the blow back damper 23 is selected so that the plug of biomass formed within the channel 6 is essentially gas impermeable when the damper head 23b is moved to an intermediate position.
[0063] The primary measuring unit 16 is adapted to measure a primary variable, in this case the electric resistance of the strain gauge, which is indicative of the gas permeability of the plug of biomass, and transmit primary variable values to the control unit 3. The control unit 3 may then use these received primary variable values to determine the gas permeability of the plug of biomass. This makes it possible for the control unit 3 to ensure that the plug of biomass is sufficiently dense and essentially gas impermeable when the damper head 23b is pushed back. The control unit 3 may, for example, be adapted to control the hydraulic or pneumatic system S to prevent the damper head 23b from being pushed back until a comparison between the determined gas permeability of the plug and an upper gas permeability threshold shows that the plug is essentially gas impermeable.
[0064] The density of the plug of biomass may vary over time, e.g. due to a change in the flow of biomass through the channel 6, and such changes may increase the risk of blow back. The main purpose of the primary measuring unit 16 is to prevent this from happening. As explained above, the electric resistance of the primary measuring unit 16 changes with the pressure applied by the plug to the inside of the housing 4, and can thus be used to determine the gas permeability of the plug. The control unit 3, which continuously receives data from primary measuring unit 16, uses these primary variable values to determine the gas permeability of the plug. If the gas permeability rises above the upper gas permeability threshold, then the control unit 3 acts to ensure that the density is increased. The control unit 3 may, for example, increase the rotational speed of the second drive mechanism M.sub.2 to increase the rotational speed of the feed screw 26 and thus increase the flow of biomass into the feeding device 2. The control unit 3 may also, or alternatively, decrease the rotational speed of the first drive mechanism M.sub.1 to decrease the rotational speed of the feed screw 12 and thus increase the pressure the plug of biomass exerts on the housing 4. Finally, the control unit 3 may regulate the hydraulic or pneumatic system S, so that the counter pressure applied by the blow back damper 23 is increased, which also moves the damper head 23b in a direction towards the outlet 10.
[0065] A change in gas pressure within the reactor 21 unit increases the risk of blow back. Therefore, the gas pressure measuring unit 22 is adapted to measure the gas pressure within the reactor 21. The control unit 3 continuously receives gas pressure values from the gas pressure measuring unit 22 and uses them to determine an optimal value for the upper gas permeability threshold, so that the upper gas permeability threshold is lowered when the gas pressure within the reactor 21 increases, and is raised when the gas pressure within the reactor 21 is reduced.
[0066] As for the system shown in
[0067] Of course, the upper and lower thresholds should be selected so that the control unit acts before blow back occurs, and/or before the channel becomes plugged.
[0068] The scope of protection is not limited by the above described embodiments and features from different embodiments may be combined in many ways. For example, the primary measuring units in