I must apologize for somewhat neglecting this blog. I've been so busy with my MBA and work. I looked at some of the analytics for this blog and noticed that the most popular post seems to those around troubleshooting. If there's anything in particular you are having trouble send me an email and I'll make sure to reply directly or present a post on the topic. I also noticed that the Cobb test troubleshooting post is the most popular post. Perhaps I should write a little bit more on this topic.
Either way I will try to pay more attention to this blog and post more often. Thanks for reading.
Thursday, September 30, 2010
Monday, July 19, 2010
Troubleshooting Tips: Worms
Worms are a formation defect resulting from strings of improperly dispersed fiber.
They can be caused by an incorrect slice setting, excessive water from the breast roll shower, and poorly set deckle boards. They can also be caused by an improperly set forming board and too high of a total head.
Once the source of the worm issue is identified the proper adjustments should eliminate the worming. If the source is not known, carefully adjust probable cause areas to identify the source. Of course, you should go through the adjustments that would cause the least possibility of a break before the ones that are more likely to cause a break.
This is a fairly straight forward process. The backtender or quality person should be the ones who detect the worms. The wetend should be notified to find the cause and rectify the situation.
They can be caused by an incorrect slice setting, excessive water from the breast roll shower, and poorly set deckle boards. They can also be caused by an improperly set forming board and too high of a total head.
Once the source of the worm issue is identified the proper adjustments should eliminate the worming. If the source is not known, carefully adjust probable cause areas to identify the source. Of course, you should go through the adjustments that would cause the least possibility of a break before the ones that are more likely to cause a break.
This is a fairly straight forward process. The backtender or quality person should be the ones who detect the worms. The wetend should be notified to find the cause and rectify the situation.
Tuesday, June 8, 2010
Back to Paper
So I've been keeping up with the news and the oil spill is still a huge problem. I apologize for not posting as much lately. There are a couple of reasons for this, I wanted to leave my oil spill solution suggestion up at the top of the blog for a while and I've been a little busy of late.
Don't worry though. I'll be posting some new stuff here in the next couple weeks. I think I will talk a little about some flex roll technology being installed for some press rebuilds. I will also try to add more troubleshooting tips as these seem to be the most popular pages. If there is anything in particular you'd like to hear about just shoot me an email.
Thank you for being a part of this blog, and I hope you've found some of the information to be helpful.
Don't worry though. I'll be posting some new stuff here in the next couple weeks. I think I will talk a little about some flex roll technology being installed for some press rebuilds. I will also try to add more troubleshooting tips as these seem to be the most popular pages. If there is anything in particular you'd like to hear about just shoot me an email.
Thank you for being a part of this blog, and I hope you've found some of the information to be helpful.
Friday, May 14, 2010
Off Topic: Oil Spill Solution
This post has nothing to do with making paper. It has to do with something much more important. The current oil spill in the Gulf of Mexico is a huge environmental issue. I have thought about the problem over the past couple of days and this is what I have come up with. My hope is that it gets in front of the right people and may provide a solution or a piece to a solution to this environmental tragedy.
I am very concerned with the current oil spill in the Gulf of Mexico. Due to this concern, I would like to offer up a possible solution. This is a rough solution that can be refined for implementation.
The current issues with siphoning the oil is the formation of natural gas (methane) hydrate. In order for this hydrate to form water needs to be present in a cold and/or high pressure environment. The phase diagram below illustrates the methane hydrate relationship between depth and temperature.
As depth increases, pressure increases. A higher pressure allows the hydrate to form at higher temperatures. For example, at 1400m (~4600ft) the temperature needs to be at or below 60F for the hydrate to form.
Figure 2 shows the water temperature at various depths for the Gulf of Mexico. At a depth of 1400m, the temperature is around 5C or 41F. At this depth and temperature, with the presence of water, hydrate will form.
The proposed solution, which is illustrated on the attached page, addresses the hydrate issue. In order to reduce or eliminate the formation of hydrate, the oil should be siphoned at a point much further away from the source of the leak. The oil must be directed so that it can be concentrated and siphoned efficiently. To direct the oil, a cylinder should be placed around the source of the leak. This cylinder can be made of concrete or steel. It needs to be able to withstand the turbulence from the outflow of oil. It also needs to be heavy enough so that it can anchor a reinforced spiral ventilation duct similar to the one shown below.
The big question mark is how long the duct needs to be. It could be anywhere from a few hundred feet to a few thousand feet. However, it does not need to come all the way up to the surface. Its purpose is to direct the flow of the oil up to a depth where hydrate formation is unlikely if not impossible so that another line which will come in from the top of the duct can efficiently siphon off the oil. The duct will act as an artificial column of oil.
The attached design of the solution shows two pumps, one for siphoning the oil and the other one near the base of the cylinder around the oil leak source. The purpose of this pump is to pump out water from the column. The specific gravity of oil is lower than water so it floats. In implementing the proposed solution, some water may be trapped in the column. While some water in the column does not present a problem, a significant amount of water will reduce the efficiency of oil recovery and also increase the possibility of hydrate formation. By pumping water out of the column near the base, this will create a column of mostly oil.
A pipe or hose should be placed inside the column with a positioning ring. This ring will keep the siphoning hose or pipe in the middle of the column. The siphoning pump should be set at a rate identical to the rate of oil leaking. Once the flows are matched up the column will achieve plug flow. Under ideal plug flow conditions, 100% of the oil coming from the leak would be recovered. However, this will be difficult to achieve without automatic controls. I believe by placing cameras near the top of the column and at various points along the column an operator could monitor and control the flow and recover over 90% of the oil. If the siphoned flow is too high water will flow in from the top of the column. If the flow is too low oil may escape through the top of the column.
The big hurdle for this solution is the design of the reinforced spiral duct. The materials necessary for a viable duct are available. However, the problem may be in the production of a duct that is long enough. While the general design of this solution seems sound, the details still need to be ironed out. Note that this is not a permanent solution, but it would alleviate the oil leak until the relief wells are operational.
If you have any questions, concerns, or comments please feel free to contact me. My email address is nhiemcao@gmail.com.
I am very concerned with the current oil spill in the Gulf of Mexico. Due to this concern, I would like to offer up a possible solution. This is a rough solution that can be refined for implementation.
The current issues with siphoning the oil is the formation of natural gas (methane) hydrate. In order for this hydrate to form water needs to be present in a cold and/or high pressure environment. The phase diagram below illustrates the methane hydrate relationship between depth and temperature.
Figure 1. Methane Hydrate Phases
As depth increases, pressure increases. A higher pressure allows the hydrate to form at higher temperatures. For example, at 1400m (~4600ft) the temperature needs to be at or below 60F for the hydrate to form.
Figure 2. Gulf of Mexico Water Depth Temperature
Figure 2 shows the water temperature at various depths for the Gulf of Mexico. At a depth of 1400m, the temperature is around 5C or 41F. At this depth and temperature, with the presence of water, hydrate will form.
The proposed solution, which is illustrated on the attached page, addresses the hydrate issue. In order to reduce or eliminate the formation of hydrate, the oil should be siphoned at a point much further away from the source of the leak. The oil must be directed so that it can be concentrated and siphoned efficiently. To direct the oil, a cylinder should be placed around the source of the leak. This cylinder can be made of concrete or steel. It needs to be able to withstand the turbulence from the outflow of oil. It also needs to be heavy enough so that it can anchor a reinforced spiral ventilation duct similar to the one shown below.
Figure 3. Ventilation Duct
The big question mark is how long the duct needs to be. It could be anywhere from a few hundred feet to a few thousand feet. However, it does not need to come all the way up to the surface. Its purpose is to direct the flow of the oil up to a depth where hydrate formation is unlikely if not impossible so that another line which will come in from the top of the duct can efficiently siphon off the oil. The duct will act as an artificial column of oil.
The attached design of the solution shows two pumps, one for siphoning the oil and the other one near the base of the cylinder around the oil leak source. The purpose of this pump is to pump out water from the column. The specific gravity of oil is lower than water so it floats. In implementing the proposed solution, some water may be trapped in the column. While some water in the column does not present a problem, a significant amount of water will reduce the efficiency of oil recovery and also increase the possibility of hydrate formation. By pumping water out of the column near the base, this will create a column of mostly oil.
A pipe or hose should be placed inside the column with a positioning ring. This ring will keep the siphoning hose or pipe in the middle of the column. The siphoning pump should be set at a rate identical to the rate of oil leaking. Once the flows are matched up the column will achieve plug flow. Under ideal plug flow conditions, 100% of the oil coming from the leak would be recovered. However, this will be difficult to achieve without automatic controls. I believe by placing cameras near the top of the column and at various points along the column an operator could monitor and control the flow and recover over 90% of the oil. If the siphoned flow is too high water will flow in from the top of the column. If the flow is too low oil may escape through the top of the column.
The big hurdle for this solution is the design of the reinforced spiral duct. The materials necessary for a viable duct are available. However, the problem may be in the production of a duct that is long enough. While the general design of this solution seems sound, the details still need to be ironed out. Note that this is not a permanent solution, but it would alleviate the oil leak until the relief wells are operational.
If you have any questions, concerns, or comments please feel free to contact me. My email address is nhiemcao@gmail.com.
Tuesday, May 11, 2010
Troubleshooting Tip: Curl
Curl is an issue that can creep up on you from time to time. There are three types of curl to be concerned with; machine direction (MD), cross direction (CD), and diagonal.
For MD and CD curl adjustments to the jet-to-wire ratio or rush/drag can be made to alleviate the issue. Generally if you are having a MD or CD curl issue, moving the jet-to-wire ratio closer to one or moving the rush/drag closer to zero will help. This adjusts the fiber orientation to alleviate the curl issue. Reducing refining and reducing broke content will also help.
Other things to look at when dealing with MD and CD curl are the size press and coater. Make sure that the sheet is picking up the same amount at the size press. The same should be done for the coater. Also check to make sure that the mixtures in the run tanks are consistent with each other. Unless you are running out of one run tank, this can be a source of trouble.
Diagonal curl is a different animal altogether. It can come seemingly out of nowhere. The first thing to look at when this issue pops up is to see what has changed. For example, was there an outage prior to the issue and if so what was changed out during the outage that could have caused the problem. The lexan sheets in the headbox can be a source of trouble. Make sure that the new sheets are the same as the old sheets and that the manufacturer hasn't changed anything in their production process. Other causes could be uneven wear of metering blades or rods at the size press. This will cause an uneven coating that could cause diagonal curl. Uneven press loading may also cause diagonal curl.
Out of the three curl types, diagonal is the most difficult to troubleshoot. Remember, curl like any other issue is caused by a change in the process. Sometimes the change is something that can be controlled, and sometimes it is due to the raw materials you have to work with. Either way make the necessary adjustment and make a note for future reference.
For MD and CD curl adjustments to the jet-to-wire ratio or rush/drag can be made to alleviate the issue. Generally if you are having a MD or CD curl issue, moving the jet-to-wire ratio closer to one or moving the rush/drag closer to zero will help. This adjusts the fiber orientation to alleviate the curl issue. Reducing refining and reducing broke content will also help.
Other things to look at when dealing with MD and CD curl are the size press and coater. Make sure that the sheet is picking up the same amount at the size press. The same should be done for the coater. Also check to make sure that the mixtures in the run tanks are consistent with each other. Unless you are running out of one run tank, this can be a source of trouble.
Diagonal curl is a different animal altogether. It can come seemingly out of nowhere. The first thing to look at when this issue pops up is to see what has changed. For example, was there an outage prior to the issue and if so what was changed out during the outage that could have caused the problem. The lexan sheets in the headbox can be a source of trouble. Make sure that the new sheets are the same as the old sheets and that the manufacturer hasn't changed anything in their production process. Other causes could be uneven wear of metering blades or rods at the size press. This will cause an uneven coating that could cause diagonal curl. Uneven press loading may also cause diagonal curl.
Out of the three curl types, diagonal is the most difficult to troubleshoot. Remember, curl like any other issue is caused by a change in the process. Sometimes the change is something that can be controlled, and sometimes it is due to the raw materials you have to work with. Either way make the necessary adjustment and make a note for future reference.
Sunday, April 25, 2010
Brighter Brights and Whiter Whites
I was thinking about something the other day, and I thought I'd share it with you. It seems like there's always a competition between paper companies to see who can make the brightest/whitest sheet. The conventional method is by adding optical brightening agents (OBAs) or optical whitening agents (OWAs) at the wetend of the machine. This seems to work fine but you can only brighten or whiten so much before you lose the effectiveness of the OBA or OWA.
So what else can you do? Well you can innovate and make a better OBA or OWA. This would require some collaboration with a chemical company and could take years to develop. So I started thinking about this and here's what I came up with.
Since the OBAs and OWAs are added at the wetend they have a limited dwell time. I wonder if increasing this dwell time would allow the OBAs and OWAs to achieve greater brightness and greater whiteness. If nothing else it could improve OBA/OWA efficiency, get more brightness or whiteness with less chemicals. So now the question is where can you add it? How far back can you go?
What about the pulp mill? Why can't it be added back there? It's definitely worth a trial right? I am not a pulp mill guy though so you should talk with your pulp mill manager to gain insight into where some good addition points might be. Also remember that if you are going from a grade the requires OBAs or OWAs to a grade that doesn't require OBAs or OWAs that it might take a little while to get all the OBAs or OWAs out of the system. Ideally you would want to try this at a mill that makes OBA/OWA required paper most or all of the time.
So the concept is to base-load the chemicals in the pulp mill and add as necessary in the wetend to reach your target brightness/whiteness.
So what else can you do? Well you can innovate and make a better OBA or OWA. This would require some collaboration with a chemical company and could take years to develop. So I started thinking about this and here's what I came up with.
Since the OBAs and OWAs are added at the wetend they have a limited dwell time. I wonder if increasing this dwell time would allow the OBAs and OWAs to achieve greater brightness and greater whiteness. If nothing else it could improve OBA/OWA efficiency, get more brightness or whiteness with less chemicals. So now the question is where can you add it? How far back can you go?
What about the pulp mill? Why can't it be added back there? It's definitely worth a trial right? I am not a pulp mill guy though so you should talk with your pulp mill manager to gain insight into where some good addition points might be. Also remember that if you are going from a grade the requires OBAs or OWAs to a grade that doesn't require OBAs or OWAs that it might take a little while to get all the OBAs or OWAs out of the system. Ideally you would want to try this at a mill that makes OBA/OWA required paper most or all of the time.
So the concept is to base-load the chemicals in the pulp mill and add as necessary in the wetend to reach your target brightness/whiteness.
Friday, April 23, 2010
Start-up Checklists
I know most people hate checklists, especially operators. They have a checklist they go through when they start-up, but usually it's in their head. Implementing formal checklists for each operator is a good way to avoid costly mistakes.
Start-ups after an outage are very hectic. Everyone has been working for a long time. They're tired and ready to go home. Having a checklist helps the operators go through the necessary steps, it also keeps the operators accountable.
So how do you go about implementing these checklist? The first step is to develop the checklist. The operators should be involved in this process so that they take some ownership of the checklist. Once the checklist is finalized, it must be determined who will actually carryout the checklist. For example a supervisor can go through the checklist with the operator to make sure that the proper steps have been taken. Simply giving the checklist for the operator to go through by themselves is not a great way to implement this tedious task. Operators would soon discard the use of the checklist and go back to their old ways. Having senior operators be responsible for the checklist would be a good way to provide some accountability.
The checklist should be turned in and kept for at least the next two outages. They should also be revised from time-to-time as new equipment is installed or modifications are made to current piping and equipment.
This is a fairly simple way to improve start-up efficiencies. Remember it's all in the way you implement the checklist. Once it is executed poorly, it will be difficult for operators to buy into the program.
Start-ups after an outage are very hectic. Everyone has been working for a long time. They're tired and ready to go home. Having a checklist helps the operators go through the necessary steps, it also keeps the operators accountable.
So how do you go about implementing these checklist? The first step is to develop the checklist. The operators should be involved in this process so that they take some ownership of the checklist. Once the checklist is finalized, it must be determined who will actually carryout the checklist. For example a supervisor can go through the checklist with the operator to make sure that the proper steps have been taken. Simply giving the checklist for the operator to go through by themselves is not a great way to implement this tedious task. Operators would soon discard the use of the checklist and go back to their old ways. Having senior operators be responsible for the checklist would be a good way to provide some accountability.
The checklist should be turned in and kept for at least the next two outages. They should also be revised from time-to-time as new equipment is installed or modifications are made to current piping and equipment.
This is a fairly simple way to improve start-up efficiencies. Remember it's all in the way you implement the checklist. Once it is executed poorly, it will be difficult for operators to buy into the program.
Thursday, April 15, 2010
Troubleshooting Tip: Ring Crush Test
The ring crush test is a method for measuring the edgewise crush resistance by forming the paper into a cylinder and applying a crushing force to the edge. For more information refer to TAPPI T818.
Linerboard products are subjected to crushing forces in handling, storage and shipment. Knowledge of the edgewise compression strength is useful in controlling the manufacturing process, and in providing an indication of the compression resistance to be expected in the finished product.
Here is a list of actions that may improve Ring:
1.Rush the sheet more or drag the sheet less.
2.Optimize refining. There should a sweet spot for ring crush. There may be times when the fiber is over refined.
3.Dry up the sheet more if possible.
4.Increase basis weight.
Realize if you dry up the sheet to improve ring crush, it may reduce your tensile strength, or burst strength. Also, increasing basis weight will increase the cost of production. However, it is better than producing broke, or reject paper. The best method for optimizing refiners is to talk to your senior stock prep operators. If they've been around for a while, they generally have a pretty good idea where to start based off refiner plate wear and the grade of paper. When adjusting the rush/drag, be sure to get your machine tenders' input. Also make sure to pay attention to the draws as this can have an effect on them, you don't want to have a break due to lack of attention to detail.
Linerboard products are subjected to crushing forces in handling, storage and shipment. Knowledge of the edgewise compression strength is useful in controlling the manufacturing process, and in providing an indication of the compression resistance to be expected in the finished product.
Here is a list of actions that may improve Ring:
1.Rush the sheet more or drag the sheet less.
2.Optimize refining. There should a sweet spot for ring crush. There may be times when the fiber is over refined.
3.Dry up the sheet more if possible.
4.Increase basis weight.
Realize if you dry up the sheet to improve ring crush, it may reduce your tensile strength, or burst strength. Also, increasing basis weight will increase the cost of production. However, it is better than producing broke, or reject paper. The best method for optimizing refiners is to talk to your senior stock prep operators. If they've been around for a while, they generally have a pretty good idea where to start based off refiner plate wear and the grade of paper. When adjusting the rush/drag, be sure to get your machine tenders' input. Also make sure to pay attention to the draws as this can have an effect on them, you don't want to have a break due to lack of attention to detail.
Monday, April 5, 2010
Troubleshooting Tip: Cobb Test
Paper is composed of a randomly felted layer of fiber, its structure has a varying degree of porosity. Therefore, the ability of fluids, both liquid and gaseous, to penetrate the structure of paper becomes a property that is very significant in the use of paper. The need to limit the spreading of ink resulted in "sizing" the paper with gelatinous vegetable materials, which had the effect of sealing or filling the surface pores. The term "sizing" was later applied to the treatment of paper stock prior to the formation of the sheet, with water-repellent materials such as rosin or wax. Resistance towards the penetration of aqueous solution / water is measured by Sizing or Cobb values.
The Cobb Test measures surface water absorption over 60 seconds, expressed in g/m2. The procedural Standards are explained in TAPPI T 441.
There are several actions you can take to improve Cobb Test numbers. An increase in refining can help close the sheet, which would improve Cobb results. A change in furnish can also help. You would increase broke content if possible and/or increase hardwood content. These fibers are smaller and can fill the holes or pores in the sheet. If you have alum at your disposal, increasing the addition rate could help. Also increasing pH can help close up the sheet. Be careful when carrying out any of these actions. You increase the risk of sealing the sheet by closing up the sheet.
The Cobb Test measures surface water absorption over 60 seconds, expressed in g/m2. The procedural Standards are explained in TAPPI T 441.
There are several actions you can take to improve Cobb Test numbers. An increase in refining can help close the sheet, which would improve Cobb results. A change in furnish can also help. You would increase broke content if possible and/or increase hardwood content. These fibers are smaller and can fill the holes or pores in the sheet. If you have alum at your disposal, increasing the addition rate could help. Also increasing pH can help close up the sheet. Be careful when carrying out any of these actions. You increase the risk of sealing the sheet by closing up the sheet.
Monday, March 29, 2010
Recycling in a Paper Mill
You would think recycling in a paper mill would be very simple, but it can be difficult at times. Most waste paper from the paper machine is recycled through the broke system. However, there are areas where it is not feasible to feed the paper back to the broke system.
I had the opportunity to optimize production in the converting area of a mill. During this optimization I noticed that there was lots of waste generated in this area that could be recycled. However, due to the mix of the paper and the location it was not ideal to sort the paper and feed it back through the broke system. The trash bins contained a few layers of paper from the rolls that were to be converted, cores, core plugs, cardboard, and other general trash.
The core plugs can be easily recylced by simply sending them back the line to be reused. The cores generally had some paper left on them and could not easily be sent back up the line to be used. So I contacted a recycler to come and do a study to see if there was enough waste for him to install a baler and provide a trailer to load the paper waste. His study concluded that the paper waste was of relatively good quality to him, and that he could install a baler and trailer at his cost and also pay the company for the paper waste that he was taking away to be recycled. This was not a large sum of money, but we would have been happy with him simply installing the baler and taking the waste away. The managers and employees were very happy with the result of the project. After the baler was installed the employees no longer had to take the waste to the compacter. The waste was compacted and baled on the floor which reduced the number of trips the forklift driver had to make from five or six per shift to just one or two. The trip was also shorter since the trailer was placed closer than where the baler location.
So look around for these opportunities. Companies are looking to be more green and sustainable, why not get paid a little bit for it. Just a thought.
I had the opportunity to optimize production in the converting area of a mill. During this optimization I noticed that there was lots of waste generated in this area that could be recycled. However, due to the mix of the paper and the location it was not ideal to sort the paper and feed it back through the broke system. The trash bins contained a few layers of paper from the rolls that were to be converted, cores, core plugs, cardboard, and other general trash.
The core plugs can be easily recylced by simply sending them back the line to be reused. The cores generally had some paper left on them and could not easily be sent back up the line to be used. So I contacted a recycler to come and do a study to see if there was enough waste for him to install a baler and provide a trailer to load the paper waste. His study concluded that the paper waste was of relatively good quality to him, and that he could install a baler and trailer at his cost and also pay the company for the paper waste that he was taking away to be recycled. This was not a large sum of money, but we would have been happy with him simply installing the baler and taking the waste away. The managers and employees were very happy with the result of the project. After the baler was installed the employees no longer had to take the waste to the compacter. The waste was compacted and baled on the floor which reduced the number of trips the forklift driver had to make from five or six per shift to just one or two. The trip was also shorter since the trailer was placed closer than where the baler location.
So look around for these opportunities. Companies are looking to be more green and sustainable, why not get paid a little bit for it. Just a thought.
Thursday, March 25, 2010
Troubleshooting Tip: Sealed Sheet
I know it has been a while since my last post, but I'm still here. I've just been busy. Anyhow, without further ado, sealing the sheet can be a very big problem. This is basically when the sheet is not draining properly. It seals itself and does not allow the water to drain. This problem can be quickly diagnosed by just looking at the sheet as it moves along the table.
Once the situation has been assessed, what do you do? There are several options. The simplest thing to do is to remove some broke. Broke contains lots of fines so reducing broke can alleviate the sealing. Another thing you can do is refine less mainly with the hardwood refiners. You can also adjust your furnish to increase softwood.
Those were the simple solutions. If none of those options helped then you've got to dig deeper. These are more machine specific options. You can increase the amount of water going to the headbox. This seems counter intuitive but in many cases this added water will create channels in the sheet to allow for improved drainage. Another option is to adjust the jet to wire ratio. This will change the fiber orientation which may help. One more option is to adjust the slice position which will change the delivery angle. This will effect other parameters such as the jet to wire ration, so be cautious when adjusting the slice. This will change where the jet lands on the forming board as well. Just be aware of the adjustments. Remember these are machine specific and may not apply to all machines.
I hope that helps. I know some of it is a little vague and general. Consult your process engineer and wet end operators before making these changes. They may have some insights that could prove useful in troubleshooting.
Once the situation has been assessed, what do you do? There are several options. The simplest thing to do is to remove some broke. Broke contains lots of fines so reducing broke can alleviate the sealing. Another thing you can do is refine less mainly with the hardwood refiners. You can also adjust your furnish to increase softwood.
Those were the simple solutions. If none of those options helped then you've got to dig deeper. These are more machine specific options. You can increase the amount of water going to the headbox. This seems counter intuitive but in many cases this added water will create channels in the sheet to allow for improved drainage. Another option is to adjust the jet to wire ratio. This will change the fiber orientation which may help. One more option is to adjust the slice position which will change the delivery angle. This will effect other parameters such as the jet to wire ration, so be cautious when adjusting the slice. This will change where the jet lands on the forming board as well. Just be aware of the adjustments. Remember these are machine specific and may not apply to all machines.
I hope that helps. I know some of it is a little vague and general. Consult your process engineer and wet end operators before making these changes. They may have some insights that could prove useful in troubleshooting.
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