this invention simplifies what has been attempted before in a very elegant aerodynamic execution of a device which not only distributes the fibers uniformly in the cross machine direction , but also allows them to be formed into a web when injected onto a forming zone and can be expanded laterally to accommodate any width of the forming zone . the key aerodynamic parameters for conveying solid particles or fibers in an air stream are well known and published in the art . the difficulty has been in developing a forming head that can maintain these conditions continuously and distribute fibers onto a forming zone at the uniformity levels and the forming zone widths desired . a forming zone in most air laid machines is a foraminous screen supported over a vacuum box to consolidate the individual fibers into a web after the air is removed . other types of forming zones are rotary vacuum drums or condensers into which the air is blown into and the fibers are condensed into a web on its surface later to be removed from the forming screen and transferred to another process operation . other forming zones are composed by air conveying and injecting the individual cellulose fibers into a curtain of molten polymeric fibers as they are extruded from the die and later consolidated in a blended form onto a forming screen or secondary forming zone . fibers or particles , because they are denser and consequently heavier than air , tend to follow their own trajectories due to the iso - kinetic forces exhibited in the air stream . therefore , it is imperative that air forming devices be designed to accommodate not only for the air characteristics required , but also accommodate the ability to uniformly convey and distribute particles or fibers in the cross direction , especially when a substrate or web is to be formed from the device and must exhibit uniformity of composition in the traverse direction . fibers , especially cellulose fluff fibers , need to be well defibrated into individual fibers and the conveying air well conditioned to prevent static and clumping . this process is well understood in the industry , with several successful designs currently in the market place . companies like kamas , m & amp ; j , and framecannica have developed devices to defibrate pulp into individual fibers for many years now . the biggest use of these fibers is in absorbent cores for disposable products such as baby diapers and feminine care sanitary products . fibers from such devices can then be conveyed by air to their final cellulose fiber forming zones . in the case of forming absorbent batts in which the thickness or basis weight of the batt is large ( greater than 100 gsm ) the aerodynamic characteristics of the fluff forming devices are not as critical . the aerodynamic and design characteristics of the forming device become much more critical when the requirement is to form a substrate of less than 100 gsm and closer to the 20 gsm level . the challenge becomes on taking fibers that are being transported in a round duct at velocities that are typically in the 1000 to 10 , 000 fpm range and spreading these fibers to widths up to five meters wide while achieving a uniformity of the fibers or particles ranging under +/− 10 % by accepted standard test methods used in measuring this parameter . the present invention uses sound engineering principles in achieving this goal . the critical parameter of this invention is to take fibers that are transported in a circular duct and spread them to widths of approximately 1 . 5 to 5 . 4 meters or greater uniformly . fig1 shows the forming head which accomplishes this goal . it is a funnel like device which is fed by a round transport duct , item 50 fig2 , which forms the inlet section . the inlet section transports a high concentration of fibers in its air stream . the spreading section of this forming head , item 70 fig2 , needs to provide air flows and fibers to the discharge section , item 60 fig2 , which are extremely uniform in the cross direction . this is accomplished by maintaining constant or slightly accelerating velocities through the funnel length with the minimum amount of turbulence , as the area of the round conveying duct is the same or slightly greater than the area of the rectangular discharge section at the end of the forming head . this concept of maintaining constant or slightly accelerating air velocities through any cross sectional plane such that aa =& gt ; bb =& gt ; cc =& gt ; dd as shown in fig1 items 10 , 20 , 30 , and 40 of the spreading section is critical in achieving uniform cross direction air profiles at the discharge of the unit . fig4 shows the air profiles that are achieved applying these techniques to the forming head . this data was obtained from an unmodified discharge section profile . meaning that the plate was flat and no adjustments to the adjusting screws were made . this air profile can be basically made totally flat when the profile control system shown in fig5 is implemented by making the adjustments to the adjusting screws , item 62 . the second key parameter is to have the fiber velocities which are equivalent to the air velocities of the conveying air stream in the transport duct be dissipated so that the iso - kinetic energy of the fiber is greatly reduced as it enters the spreading section . this is accomplished by the geometry of item 50 of fig2 , which shows the round duct entering the funnel at an angle , thus having the fibers hit the far wall of the spreading section . in this manner the velocity of the fibers and the momentum of the fibers are dissipated . this allows the fibers then to be re - aligned with the airflow profiles in the spreading section that will be developed by the geometries and air velocities used in the design of this spreading section . if this step is not done , the fibers would have the tendency to stay in the center of the spreading section creating a heavier center on the substrate formed . the angle of the circular duct to the spreading section can vary , as long as the fiber velocity is dissipated as they strike the back wall of the spreading section . the angle in which the circular duct enters the funnel will depend on the height to width ratio of the funnel itself such that this angle can vary from 15 ° to 90 °, but will be closer to 45 ° in most typical applications . other means of transporting the fibers to the entrance of the forming head such as venturi inlets can be contemplated so that the velocities of the individual fibers can align themselves with the velocities of the air stream . once the fibers are in the spreading section , it is important that they have enough residence time in this section to streamline themselves to the airflows that have been developed within the section . this is accomplished by having the height of the spreading section be at a minimum equivalent to ten times the diameter of the round transport duct for the fibers . lengths much shorter than 10 equivalent diameters will result in less efficient fiber spreading in the cross direction and unacceptable profiles . as there may be physical limitations to optimizing the spreading section to heights greater than 10 equivalent diameters or greater of the width of the inlet duct , the angle of the fiber inlet to the wall of the funnel will need to be adjusted accordingly to accommodate this relationship . the third key element of this invention is the ability to control the discharge of the fibers onto a forming zone such as a foraminous forming screen or onto another fiber stream in order for the fibers to blend with these fibers forming a web and provide acceptable formation . in this case the angle in which the fibers are directed onto either type forming zone is critical . this angle may require adjustment . item 60 in fig2 shows a device which is used as the discharge section for the spreading section to turn the fibers in the proper direction . the figure shows a nozzle with a 90 ° turn . this angle can be varied and can be whatever the final forming zone application requires it to be . besides designing the discharge with a specific angle , a method that can be used to vary this angle is to tilt the spreading and forming head to that angle which will be required for proper web forming . another critical advantage that this system has is its ability to have modular forming units . thus , these forming devices can be combined individually in the cross machine direction making the formation width of the machine to any width desired . fig3 shows the advantage of this design by showing two side - to - side spreading sections items 70 and 70 ′. there is no limitation to the number of spreading sections with their respective inlet sections that can be added in the cross machine direction making it possible to achieve widths of five meters or more . for practical purposes , the ideal width of the individual forming heads are in the range of 1 to 1 . 5 meters . even though the spreading sections with their respective inlet sections are separate units , their discharge portion , item 60 in the figures shown , is a continuous , monolithic , unitary section . in this manner , the fibers are air formed with uniform cross direction when injected into the final forming zone without any separation as a result of combining the separate spreading sections through the unitary discharge section . furthermore , the discharge section as is shown in fig5 , item 60 , has an adjustable bottom plate , item 61 , which can be constricted in opening by adjustable screws , item 62 , to influence the trajectory of both the fiber and air stream . this added control system controls for a uniform profile of fibers into the forming zone . the plate material is made of a soft , flexible metal or plastic which bends as stress is applied via turning screws such as shown in item 62 illustrated in fig5 , in the cross - section of the discharge section of the forming head . the adjustment of the plate at this juncture is relatively small , thus creating restrictions to the discharge opening in the vicinity of 0 . 25 to 0 . 75 inches . these restrictions serve to accelerate the discharge air and as a result force the fibers to spread out in that particular location allowing for the basis weight to be adjusted . adjustments made by this technique result in a correction of +/− 3 grams per square meter to the final fibrous substrate being formed , and are used as a means to fine tune any irregularities to the basis weight profile . the effect of the discharge section adjustment plate is optimized by the curvature of the full width monolithic discharge section item 60 fig2 . the curvature of this section tends to have the fibers in the airstream hug the bottom wall of the discharge section as a result of the iso - kinetic and centrifugal forces exhibited , thus making the fibers more susceptible to movement and redistribution in the airstream as a result of the adjustments made to the bottom discharge plate . as the angle of the discharge can vary depending on the nature of the forming zone that the fibers are being injected into , the effectiveness of the control exhibited by varying the gap of the discharge outlet is impacted . consequently , the control originally exhibited on a discharge outlet with a 90 ° outlet is reduced . as the angle can be increased from 90 ° to 180 °, the fibers would then become much better distributed through the entire cross - section of the discharge section rather than hug the bottom wall as they would with a 90 ° outlet angle . consequently , a further improvement to this control device was developed , which would allow for the control of both fiber and air distribution by constricting the outlet of the discharge from both the top and the bottom walls of the discharge section as shown in fig6 . in this manner the velocities of the air stream could be further increased in certain regions in the cross direction , making the control of the adjustments as great as +/− 5 gsm in the cross - direction of the web .