The present invention relates to the field of kilns used in the continuous drying of lumber, and more particularly pertains to an improved kiln having a continuous green lumber feed and dry lumber discharge stream.
As is well known, fresh cut lumber includes a large quantity of moisture and it has been the practice to subject such lumber to heat treatment to drive off the moisture so that the lumber, as sold, will be less subject to warping or bending during storage or after installation in a structure.
Drying lumber is typically performed in a batch kiln process, where an insulated chamber is used that is adapted to control several drying process conditions, including, but not limited to air temperature in the kiln, air speed across the lumber, and the relative humidity in the chamber. As these kilns are a closed atmosphere, packages of sawn lumber, often referred to as green lumber, separated by stickers are placed in the kiln in batches. The packages are often loaded vertically, horizontally, and end to end.
Once the batch of packages are in place, the chamber is closed and a schedule or recipe of temperatures and relative humidity is initiated for a determined time interval or until a certain moisture content in the lumber is achieved. Generally, the schedule gradually increases the temperature in the chamber and lowers the relative humidity. This allows the lumber to give up its moisture to the surrounding air, which may then be vented to the outside atmosphere.
The particular schedule used and the drying time varies depending on a number of factors, including, but not limited to, lumber type/species, thickness, moisture content, end use of the lumber and the like. Once the schedule has run, the kiln doors are opened and the packages are removed from the kiln chamber and further prepared for shipping to a final destination. This opens the chamber to atmospheric conditions and can often require a significant amount of time and energy to bring the next charge of green lumber up to drying conditions.
While lumber is typically dried as fast as possible depending on the cell structure, drying too rapidly can have adverse effects on the lumber, such as checking, splitting, warping, cupping, and the like. Accordingly, the temperature and humidity in the kiln, as well as the drying time will vary depending on the above listed factors. For example, Red Oak may take up to 28 days dry from green to 7% moisture content, while Southern Yellow Pine can be dried in approximately 20-24 hours from green to 15% moisture content.
As described in U.S. Pat. Nos. 7,963,048 (Pollard), 8,201,501 (Tinsley), and 8,342,102 (Tinsley), the complete disclosures of which are incorporated by reference herein, disclose the use of two generally parallel paths for separate continuous drying lines which are moved in opposite directions through a plurality of chambers which are aligned along the separate paths and in communication with one another to increase the efficiency of the drying process. This is accomplished by continuously moving loads of lumber while conserving the heat that builds up in each load as it is continuously moved along one path in the kiln and transferring some of that heat from a load of dried lumber to an incoming load of green lumber moving from the opposite end of the kiln as they pass one another in the kiln.
Prior art dual path kilns utilize internal reversible propeller fans because the flow of air through the lumber in central heating chamber must be periodically reversed, typically every three hours. Many of the prior art kilns also reverse the flow of air through the lumber in each of the end chambers. While the air flow through the lumber is being reversed, the lumber is not being dried. Furthermore, reversible fans are mechanically inefficient compared unidirectional fans. Moreover, since the fans are inside the hot central chamber they are fully exposed to a harsh environment.
There is a need for a continuous kiln that does not have the losses in productivity associated with fan reversals and can be used continuously to dry the lumber. There is also a need for a continuous kiln that can use single direction fans.
An objective of the invention is to provide a kiln that does not have to reverse the air flow through the lumber and also can utilize more efficient single direction external fans that are not externally exposed to the harsh environment in the central heating chamber.
The above objectives and other objectives can be obtained by a continuous kiln comprising:
The above objectives and other objectives can also be obtained by a method of continuously drying lumber in a kiln comprising:
The objectives and other objectives can further be obtained by a continuous kiln comprising:
The above objectives and other objectives can be obtained by a method of continuously drying lumber in a kiln comprising:
The operation and advantages of the present invention will become apparent as consideration is given to the following detailed description in conjunction with the accompanying drawings, in which:
In the following detailed description, reference may be made to the accompanying drawings which form a part hereof, and in which is shown by way of illustration embodiments in which the invention may be practiced. It is to be understood that other embodiments may be utilized and structural or logical changes may be made without departing from the scope of the present invention. Therefore, the following detailed description is not to be taken in a limiting sense, and the scope of embodiments in accordance with the present invention is defined by the appended claims and their equivalents.
Embodiments of the present invention are directed to a kiln 1 that can be used to perform a continuous type lumber drying process, where, in
The kiln 1 comprises three chambers, a first end chamber 6, a central heating chamber 2 and a second end chamber 10. Each of the chambers 2, 6 and 10 comprise walled structures defining an enclosure so that conditions within the chambers 2, 6, 10 can be controlled, such as air flow, temperature, and humidity. Each of the enclosures 2, 6 and 10 have openings for the conveyors 12, 14 to continuously convey lumber through the chambers 2, 6 and 10. Chambers 2, 6 and 10 are now well known and any suitable structures for the chambers 2, 6 and 10 can be utilized. The present invention is an improvement over conventional continuous dual path kilns 1 having chambers 2, 6 and 10. The kiln 1 can include any number additional chambers as desired. The chambers 2, 6 and 10 can be divided into sub chambers, for example as shown in the
The first end chamber 6 has a first kiln opening 4 and the first end chamber 6 is connected to the central heating chamber 2. The second end chamber 10 is has a second kiln opening 8 and the second end chamber 10 connected to the central heating chamber 2. A first baffle 7 separates the first end chamber 6 from the central heating chamber 2. A second baffle 9 separates the second end chamber 10 from the central heating chamber 2. The baffles 7 and 9 separate the heating air in the central heating chamber 2 from the air in each of the end chambers 6 and 10, and allow the lumber on the conveyors 12, 14 to travel through each of the chambers 2, 6 and 10. Preferably, the baffles 7 and 9 each comprise a wall from the ceiling to the floor in the chambers 2, 6 and 10, with openings for the conveyors 12, 14, an example of which is shown in
The central heating chamber 2 can be divided by a central heating divider 50 into to a first heating chamber 52 and a second heating chamber 54. The first end chamber 6 can be divided by a first end divider 60 into a first treatment chamber 62 and a first heat transfer chamber 64. The second end chamber 10 can be divided by a second end divider 66 into a second treatment chamber 70 and a second heat transfer chamber 68. The dividers 50, 60 and 66 preferably separate air flow in a upper portion of the chambers 2, 8 and 10. The dividers 50, 60, and 66 can comprise a wall from the ceiling to the floor in the chambers 2, 6 and 10, with openings for the conveyors 12, 14. However, preferably the dividers 50, 60 and 66 comprise a wall from the ceiling to a height above the floor, as shown in
Any suitable conveyor 12 and 14 can be utilized to convey the lumber through the kiln 1. Preferably, the first conveyor 12 comprises a set of rails upon which a first carriage 16 having wheels 20 rides, and the second conveyor 14 comprises a set of rails upon which a second carriage 18 having wheels 20 rides. The first carriage 16 holds a first charge of green lumber 22 and is pushed on the rails by a pusher device 28. The second carriage 18 holds a second charge of green lumber 24 and pushed on rails by another pusher device 28. The first conveyor 12 conveys the green lumber 22 through the kiln 1 in the following order, through first entry opening 4 into the first treatment chamber 62, the first heat transfer chamber 64, the first heating chamber 52, the second heating chamber 54, the second heat transfer chamber 68, second treatment chamber 70, and then out the second entry opening 8. The second conveyor 14 conveys the green lumber 24 through the kiln 1 in a direction opposite the first conveyor 12, in the following order, into the second kiln opening 8 into the second treatment chamber 70, the second heat transfer chamber 68, the second heating chamber 54, the first heating chamber 52, the first heat transfer chamber 64, the first treatment chamber 62 and then out the first kiln opening 4. Once the green lumber 22 leaves the central chamber 2 it is considered dry lumber 25. Once the green lumber 24 leaves the central chamber 2 it is considered dry lumber 26.
The first end chamber 6 has at least one external first end fan 40 configured to provide a first end flow of air in the first end chamber 6. The fan 40 is preferably a centrifugal fan having an inlet 42 and outlet 44. The centrifugal fan 40 is unidirectional and non-reversible. Preferably, the first end chamber 6 has at least two fans 40 so that if one fan 40 is offline for repair or maintenance the other fan(s) 40 can continue to provide necessary air flow. The fan 40 is preferably configured to provide the first end flow of air in the direction from the dry lumber 26 on the second conveyor 14 towards the green lumber 22 on the first conveyor 12. As shown in the
The second end chamber 10 has at least one external first end fan 40 configured to provide a second end flow of air in the second end chamber 10. The fan 40 is preferably a centrifugal fan having an inlet 42 and outlet 44. The centrifugal fan 40 is unidirectional and non-reversible. Preferably, the first end chamber 10 has at least two fans 40 so that if one fan 40 is offline for repair or maintenance the other fan(s) 40 can continue to provide necessary air flow. The fan 40 is preferably configured to provide the second end flow of air in the direction from the dry lumber 25 on the first conveyor 12 towards the green lumber 24 on the second conveyor 14. As shown in the
The central heating chamber 2 has at least one fan 40 to provide a heating air flow. Preferably, each of the first and second heating chambers 52 and 54 have associated fans 40. As shown in
The fans 40 are preferably centrifugal fans. The centrifugal fan is now well-known and any suitable centrifugal fan can be utilized. The centrifugal fan is a mechanical device for moving air and/or other gases. The fan increases the speed and volume of an air stream with the rotating impellers. Centrifugal fans use the kinetic energy of the impellers to increase the volume of the air stream, which in turn moves them against the resistance caused by ducts, dampers and other components. Centrifugal fans displace air radially, changing the direction (typically by 90°) of the airflow. They are sturdy, quiet, reliable, and capable of operating over a wide range of conditions. Centrifugal fans are constant displacement devices or constant volume devices, meaning that, at a constant fan speed, a centrifugal fan moves a relatively constant volume of air rather than a constant mass. This means that the air velocity in a system is fixed even though the mass flow rate through the fan is not. The centrifugal fan is a drum shape comprising a number of fan blades mounted around a hub (impeller). The hub turns on a driveshaft mounted in bearings in the fan housing. The air/gas enters from the side of the fan wheel, turns 90 degrees and accelerates due to centrifugal force as the air/gas flows over the fan blades and exits the fan housing. The direction of flow through the centrifugal fan cannot be reversed. Examples of centrifugal fans that can be utilized comprise a model IAP Size 600 ‘B’ Class II fan, 65,000 CFM, operating speed 509-, 40 HP motor. Another example is an IAP Size 730 ‘A’ Class II fan, 110,000 CFM, operating speed 440 RPM, 60 HP motor.
Different horsepower/sized fans may be used in different zones to controllably vary the rate of air flow through the lumber charges. The baffles 7, 9 and dividers 50, 60, 66 help prevent migration of air velocity and help maintain air differentials between the zones. In one embodiment, the higher air velocity is generated in the zones at or near the center of the kiln 1. The air velocity may be gradually reduced in the zones towards the entry/discharge ends of the kiln 1.
The kiln 1 can be operated such that a continuous dried lumber charge 26 exits the first opening 4 of the kiln 1 while a continuous green lumber charge 22 enters the first opening 4, and at the opposite end of the kiln 1 a continuous dried lumber charge 25 exits the second opening 8 of the kiln 1 while a continuous green lumber charge 24 enters the second opening 8.
Embodiments allow for the heat dissipating from the dried lumber 25, 26 after exiting the central heating chamber 2 to heat or preheat the green lumber 22, 24 in the end chambers 6, 10, thereby saving time and energy over the batch kiln systems. Embodiments also include the green lumber 22, 24 releasing moisture into the air due to the heating by the dried charge 25, 26, which cools the air and may assist in conditioning the dried lumber 25, 26 prior to exiting the kiln 1.
The kiln 1 includes a heater 120 for heating any of the chambers 2, 6 and 10. The heater can provide direct and/or indirect heat as desired. Heaters 120 are now well-known and any desired heater can be utilized. The heater 120 can be located outside of the kiln 1 and can supply heated air through an associated fan and duct system to the central heating chamber 2, and/or any other part of the kiln 1 as desired.
The kiln 1 can include a computer system 100 to control the operation of the kiln 1, including speed of the pushers 28, speed of the fans 20, conditions in the chambers 2, 6 and 10, such as temperature and humidity, and any other operations as desired. Computer systems 100 and associated controls are now well known and any desired computer system 100 and control can be utilized in the kiln 1 as desired.
Embodiments of the present invention are directed to a continuous type lumber drying process, where, in
Preferably the green lumber charges 22, 24 loaded on the carriages 16, 18 and are moved in opposite directions at rates appropriate to drying characteristics of the lumber products comprising the charge through the kiln 1 using pushers 28, and are controllably moved at a rate calculated to ensure that the proper drying of a green charges 22, 24 is achieved from the time it enters one end 4 or 8 and exits the opposite end 4 or 8 of the kiln 1. Multiple carriages 16, 18, may be linked together in such a way that they can be pushed by pushers 28 to effect the desired movement with the pushing being effective to eliminate or reduce spaces between the carriages when several carriages 16, 18 are being used.
The construction, dimensions, sizing and control of the chambers 2, 6 and 10, carriages 16, 18, and pusher devices 28 can be as conventionally used in known dual path kilns 1. The present dual path kiln 1 is an improvement over conventional dual path kilns. In the present kiln 1, more efficient centrifugal fans external to the kiln are utilized. It was not known prior to the present invention that unidirectional and external fans, like the centrifugal fans, can be utilized in a dual path kiln 1. It was believed that internal propeller type fans were required so that the air flow directions could be periodically reversed. Applicant has found that surprisingly, consistent circular air flows through the lumber can be utilized to effectively and more efficiently dry lumber in a dual path kiln 1, without having to reverse the air flow direction. However, the air flow directions, number of the air flows, placement of the air flows and velocities described herein and shown in the drawings are exemplary and any flow direction, number of air flows, placement of air flows and velocities can be utilized as desired for the particular kiln application.
Conventional dual path kilns can now be upgraded with the external unidirectional fans 40, ducting and control systems as described herein to provide unexpectedly improved lumber drying rates and thus lumber drying cost savings.
If desired, additional ducts and valves can be added so that fans can be connected to more than one chamber, so that if one fan is shut down another fan can be utilized to provide air flow elsewhere in the kiln 1. Preferably, there is little or no air flow in the first and second treatment chambers 62 and 70.
A preferred method of continuously drying lumber using the kiln 1 comprises pushing a charge of green lumber 22 into the opening 4 into the first treatment chamber 62, the first heat transfer chamber 64, the first heating chamber 52, the second heating chamber 54, the second heat transfer chamber 68, second treatment chamber 70, and then dry lumber 25 out the second entry opening 8. The method also comprises pushing a charge of green lumber 24 through the kiln 1 in a direction opposite the first conveyor 12, in the following order, into the second kiln opening 8 into the second treatment chamber 70, the second heat transfer chamber 68, the second heating chamber 54, the first heating chamber 52, the first heat transfer chamber 64, the first treatment chamber 62 and then dry lumber 26 out the first kiln opening 4.
As the green lumber charges 22, 24 pass the dried lumber charges 25, 26 in the end chambers 6, 10, the dried charges 25, 26 heat the air in the end chambers 6, 10. This heating effect in turn can heat the green lumber 22, 24, thereby gradually raising the temperature encountered by the green lumber 22, 24 and initiate the drying process of the green lumber. Likewise, as the green lumber 22, 24 begins to dry, it can release moisture into the air of end chambers 6, 10. This moisture release may cool the air and increase the humidity of the air.
The kiln 1 can be vented through the open ends 4, 8. Alternatively, one or more vents may be positioned in any of the fan outlet ducts 44 to controllably regulate the temperature and manage any condensation or moisture congregation that can occur.
The travel time of the lumber charges 22, 24 through the kiln 1 may vary depending on many of the same factors affecting the batch kiln process. When using a continuous drying process in accordance with embodiments of the present invention, the length of time for the lumber 22, 24 to pass through the kiln 1 and be dried to a desired moisture content can be similar to the typical batch kiln process for analogous species and dimensions. It is preferred that the travel rates the charges 22, 24 pass through the kiln at collectively or independently varying rates depending on the rate of drying for the lumber products that comprise the charge, but opposite in direction. Accordingly, the moisture content of the lumber charges being dried can monitored by the computer system 100, and the pusher 28 rate as reflected in the velocity of the carriages 16, 18 traveling on rails in each path 12 and 14 can be altered as needed to ensure the dried lumber charges 25, 26 exit the kiln at the proper moisture content.
Examples: The invention will be further explained by the following non-limiting exemplary processes.
In an example, the environment in the treatment chambers 62 and 70 is saturated, with both the wet bulb (WB) temp and the dry bulb (DB) temp at about 100 to 120° F. As the green lumber 22, 24 moves through the first 10 feet of the treatment chambers 62 and 70, the DB and WB temps rapidly increase to about 150 to 160° F. As the charges 22, 24 leave the initial 10′ of the treatment chambers 62, 70, the DB temp increases linearly through the heat transfer chambers 64, 68, and the WB temp remains essentially the same. At the transition from the heat transfer chambers 64, 68 to the center chambers 52, 54, the DB temp is ˜190° F.-200° F., and the WB temp is ˜150° F.-160° F. When the lumber 22, 24 enters the center chambers 52, 54, the DB temp immediately increases to the kiln set point temp (˜210° F.-260° F.), while the WB temp remains at the same temp as it was upon reaching the center chamber 2. These temps remain essentially constant as the lumber 22, 24 makes its way through the entire center chamber 2. The green lumber 22, 24 becomes dry lumber 35, 26 upon leaving the center chamber 2.
Relative Humidity for each chamber: In the treatment chambers 62, 70, the environment in the kiln is saturated, and the Relative Humidity is about 100%. As the lumber 22, 24 moves through the first about 10 feet of the kiln 1 in the treatment chambers 62, 70, the Relative Humidity remains at about 100%. As the lumber 22, 24 leaves the treatment chambers 62, 70, the relative Humidity decreases linearly through the remainder of the chamber, and at the transition from the initial end chamber 6, 10 to the center chamber 1, the Relative Humidity is about 60-70%. When the lumber 22, 24 enters the central heating chamber 2, the Relative Humidity immediately decreases to about 20-30%. These humidity conditions remain essentially constant as the lumber 22, 24 makes its way through the entire center chamber 2.
Circulation air flows shown in
Lumber Indexing rate ranges: Indexing rate is related to the dimensional characteristics of the lumber 22, 24 being dried in that lumber 22, 24 exhibiting “high total surface area to volume” ratios index faster than lumber 22, 24 with lower ratios. Indexing rate is also directly related to the overall length of the central heating chamber 2 of the kiln 1, inasmuch as the total residence time of the lumber 22, 24 in the central heating chamber 2 of the kiln 1 is constant irrespective of central heating chamber 2 length. As such, longer central heating chamber 2 kilns exhibit higher pack indexing rates. Indexing rate, is related to the DB set point temp of the kiln 1, as higher set point temps yield higher indexing rates. Indexing rates can vary from about 1 foot per hour to about 10 feet per hour travel of the lumber 22, 24 on the conveyors 12, 14, depending on the factors outlined above.
It is not an obvious design choice to replace internal reversible propeller fans with external unidirectional fans. The prior art kilns require periodic reversal of the flow directions, which could only be accomplished with the internal reversible propeller fans. It has now been surprisingly found that faster and improved drying of the lumber can be accomplished by a new structure of the kiln using constant air flow directions in which reversible fans are no longer required. Thus, the external single direction fans can now be utilized in place of conventional reversible fans.
The fans preferably provide a circular air flow through the lumber and above the lumber as shown in
A major difference between the present invention and the Counterflow Dual Path Kiln disclosed in U.S. Pat. No. 7,963,048 (Pollard) Pollard include the circulation air direction in the present kiln 1 is not required to reverse. In the prior art, the air flow through the lumber is periodically reversed. In an example of the present method, for the entire length of the kiln—the circulation air flow directions do not ever change in the partitioned chambers. Because the air flows are not required to reverse, the circulation fans are not typical propeller type fans located internal to the kiln and above the fan deck, but rather are centrifugal type fans that are external to the kiln structure, have a far higher efficiency, are fewer in number and can be located at ground level. Prior to the present invention, centrifugal fans have not been used to generate circulation air in a dual path continuous kiln.
The first end chamber 106 has two associated first end chamber fans 144 and 146, having inlets into the first end chamber 106, so that the air flows through the green lumber 22, then through the green lumber 24, and then into the inlets of the fans 144, 146. The second end chamber 110 has two associated second end chamber fans 140, 142, having inlets into the first end chamber 110, so that the air flows through the second dry lumber 26, then through the first dry lumber 25, then into the inlets of the fans 140, 142. The outlets of the fans 140, 142 flow air from the second end chamber 110 to the first end chamber 106. The outlets of the fans 144, 146 flow air from the first end chamber 106 to the second end chamber 110. In this manner, the fans 140, 142, 144 and 146 provide a circular air flow through the lumber in the first end chamber 106 and second end chamber 110. Ducts are now well known and any desired ducts can be utilized to provide the air between the fans 140, 142, 144 and 146 and the chambers 106, 110.
The first center chamber 52 has two associated first center chamber fans 152, 154, having inlets into the first center chamber 52, so that the air flows through the second green lumber 24, then through the first green lumber 22, then into the inlets of the fans 152, 154. The second center chamber 54 has two associated second center chamber fans 148, 150, having inlets into the second center chamber 54, so that the air flows through the first green lumber 22, then through the second green lumber 24, then into the inlets of the fans 148, 152. The outlets from the fans 148, 150 flow air from the second central chamber 54 to the first central chamber 52. The outlets of the fans 152, 154 flow air from the first central chamber 52 to the second central chamber 54. In this manner, the fans 148, 150, 152, and 154 provide a circular air flow through the lumber in the first central chamber 52 and second central chamber 54. Ducts are now well known and any desired ducts can be utilized to provide the air flows between the fans 148, 150, 152 and 154 and the chambers 52, 54.
The invention will be further described with reference to the following Examples. Since the circulating air flow occurs solely within the chamber it is serving and moves outside of the kiln structure proper and passes through ducting into and out of the centrifugal fan, this makes it much more practical to install a conventional very early warning fire protection systems (an example of which is an aspirating smoke detection system, see: https://www.systemsensor.com/en-us/_layouts/ss/search.aspx?k=Aspiration-Conventional-Detectors). Prior art dual path kilns do not have this chambered air flow, nor do they have provisions for ready access to the flow outside the kiln structure proper.
In a prior art dual path kiln, when the fans reverse, the circulating air flow stops briefly (2-5 minutes) and does not return to optimum velocities for significantly longer than that, so in addition to “not drying” in that interval, the heat load required of the heating system for the kiln drops dramatically and the temperature in the kiln rises significantly (˜50-70 degrees F.). Without being bound by any theory, it is believed that when drying pine lumber, the emission rate of hazardous compounds as defined by the EPA (Volatile organics—“VOC's”—and non-criteria Hazardous air pollutants—“HAP's”—formaldehyde and methanol) rise dramatically . . . when the fans don't reverse, the temperature spikes are eliminated and kiln emission levels unexpectedly drop. Another significant benefit from not reversing the fans is that since fan reversals are not occurring, the heat load for the kiln remains very consistent and the heat source can surprisingly be operated at a much higher level of efficiency. In direct heated (i.e slope grate sawdust burner) kilns, the more consistent demand for heat heat is especially beneficial as direct heated kilns do not react to rapid changes in heat load well.
Emission and production testing was conducted at Charles Ingram to compare their prior art kiln #5 (conventional DPK) to the present invention kiln #6 (NOREV DPK). During the emissions testing, drying productivity was tracked. The “time lost drying” due to fan reversals in a conventional DPK, or the increase in drying rate from a NOREV DPK was a surprising and unexpected 10%. Emissions testing comparing the two kilns was also conducted. To summarize NOREV DP Kiln #6 according to the present invention exhibited numerous unexpected and surprising advantages compared to the prior art DP Kiln 5. For the HAP formaldehyde, NOREV DP Kiln #6 emission levels were a surprising and unexpected 20% lower than DP Kiln #5. For the HAP methanol, NOREV DP Kiln #6 emissions levels were a surprising and unexpected 20% lower than DP Kiln #5. For the criteria pollutant VOC's, NOREV DP Kiln #6 emission levels were a surprising and unexpected 59% lower than DP Kiln #5.
Table 1 lists the Dual path continuous kiln specifics for the prior art Kiln #5.
Table 2 lists the Dual path continuous kiln process data results for the prior art Kiln #5.
Table 3 lists the Dual path continuous kiln process data results for the prior art Kiln #5.
Table 4 lists the Dual path continuous kiln process data results for the prior art Kiln #5.
Table 5 lists the Dual path continuous kiln specifics for the Kiln #6 operated according to the present invention.
Table 6 lists the Dual path continuous kiln process data results for the Kiln 6 according to the present invention.
Table 7 lists the Dual path continuous kiln process data results for the Kiln #6 according to the present invention.
Table 8 lists the Dual path continuous kiln process data results for the Kiln #6 according to the present invention.
The test results demonstrate a drying productivity improvement of the present invention Kiln #6 over the prior art Kiln #5 of an unexpected and surprising 110%.
In addition to the discussion of various embodiments above, figures and additional discussion are presented herein to further describe certain aspects and various embodiments of the present invention. It is to be understood, however, that a wide variety of alternate and/or equivalent embodiments or implementations calculated to achieve the same purposes may be substituted for the embodiments shown and described without departing from the scope of the present invention. Those with skill in the art will readily appreciate that embodiments in accordance with the present invention may be implemented in a very wide variety of ways. This application is intended to cover any adaptations or variations of the embodiments discussed herein.
Number | Date | Country | |
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62623080 | Jan 2018 | US |