START-UP
The CP-4 press runs on single phase current, 110 volts. It is provided with a reversing switch so that the direction of rotation can be selected. The screw of the press turns in a counterclockwise direction, when viewed from the drive end of the press.

Alternatively, the press can be supplied with motor options such as 208-220 volt single phase, three phase, 380-580 volt, explosion proof. Extended length inlet hoppers and 316 stainless steel construction are available.

To suit individual situations, the press can be installed tilted upwards. Also, the gearbox can be rotated 90º or 180 o. Consult the factory in these situations as the oil level in the gearbox may have to be adjusted.

Before putting power to the screw press it is advisable to rotate the screw by hand or at least to bump the motor. This will prevent damage to the press in case the screw has shifted so as to hit the screen. Also, the presence of tramp material in the press will be revealed. To turn the screw by hand, remove the fan guard on the motor and turn the fan blades.

INSTRUMENTATION
The most useful instrument to have when testing a press is an ammeter. The load drawn by the drive motor of the press is indicative of how much work the press is doing. The higher the amps, the better the dewatering. Also, the higher the amps, the closer the press is to jamming and the greater the abrasive wear. Very low amps indicate little dewatering is being done; the screen is blinded; or low compression is taking place.

A moisture balance is valuable for measuring the moisture content of the inbound material and of the press cake. If an oven is used to dry samples, be sure it is set at 200º F or less. Samples should be left in the oven overnight. The tare weight of the pan should be much less than the weight of the sample which is being dried.

In the case of pressing liquids that contain dissolved sugars, a refractometer is valuable for assessing press performance. The Brix of the inbound flow, the press cake, and the press liquor will all be the same figure. The higher the Brix, the lower the moisture content of the press cake.

If dissolved (soluble) solids are present, the suspended (insoluble) solids (fiber) in the press liquor are generally measured by filtering and washing a sample and drying the filter paper in an oven. Dissolved solids will be washed from the sample during the washing process.

FEEDING
Material can be fed into the press many ways. Pouring from a 5-gallon pail is most common for the CP-4 press. In pilot or production runs, screw conveyors, pumps, transition chute, or cyclone separators are used. Always allow for return feed of overflow material in the event that more is fed to the press than it can take. Spill containment is a consideration.

Sometimes either a static (sidehill) screen or a rotary drum screen (RDS) is mounted over the inlet hopper to prethicken the flow ahead of the press; the tailings (solids) from the screen are funneled into the press. This arrangement is desirable when the feed to the press is dilute.

Also, material can be dropped from a shredder or cyclone separator into the press. A shredder is used to prevent jamming and to increase capacity and dewatering in the case of low bulk density materials like lettuce leaves, alfalfa, onion peel, and cornhusk.

Most commonly, the best screw press performance is achieved if the material in the inlet hopper stays just at the top edge of the screw. Usually presses work the best with only atmospheric pressure in the inlet hopper. In order to minimize static head, press headboxes are kept short, and level controls are used to minimize the depth.

When a pump is used, the system can be either open or closed. We recommend the open system where little or no pressure exists in the inlet hopper, thus preventing the press from being force-fed. In this arrangement either there is an open return line allowing flow back to the source feeding the press, or level is controlled in the inlet hopper. It is best to have a line that allows material to recirculate past the press inlet. This will prevent pressurizing the inlet of the press, which can cause both blinding of the screen and purging from the cake discharge.

If the feed flow is piped through a sealed cover which is bolted to the inlet hopper, force-feeding is possible. A by-pass tee should be provided so that the pressure in the inlet hopper is minimized. In addition, a 2" vent line, open to the atmosphere, must be provided to prevent siphoning material in the inlet hopper out through the recirculation line.

Inlet hopper pressure over one to four psi can force solid material against the screen so as to blind off the screen, resulting in unsatisfactory performance.

At pressures above 10 to 15 psi in the inlet hopper, it is possible to blow the "plug" of press cake that forms at the discharge of the press. Unscreened liquid will purge from the cake discharge. Exercise extreme caution if either hot or hazardous material is being pumped into a press.

At pressures of 40 psi and above the shaft seals will be blown out of their housing. At pressures around 60 psi the screen will start to separate from its support plates, resulting in bypassing of feed material directly into the press liquor flow.

BUILDING A PLUG
In order for the press to work, a plug of cake must be formed between the cake discharge and the cone. The press will almost always do this on its own accord as material is fed into the press.

In the case of sloppy materials like manure and DAF sludge, it may be advisable to start off by first packing the discharge of the press with any available fibrous material.

Alternatively, the press can be turned on and the feed pump allowed to run just long enough to fill the feed line and the press. Then shut off the pump and wait until no more liquid drains from the screen of the press. Repeat this process about four times until a plug of cake starts to open the cone.

PRE-THICKENING
In general, the thicker a flow going into a press, the better it will work.

If the flow into a screw press is too dilute, the high volume of liquid going through the press screen can cause either of two problems. The flow may either flush most of the solids through the screen, or it may plaster solids against the screen, thus blinding (covering over) the screen. To prevent these things from occurring, it may be necessary to pre-thicken the flow ahead of the screw press. This is commonly done with a static screen (sidehill) or a rotary drum screen (RDS). In the case of very dilute feed to the press, a Fiber Filter can be used.

AIR CYLINDER REGULATOR
Presses are supplied with an FRL set (filter, regulator, lubricator), along with a Parker four-way reversing valve. These should be installed near the cone end of the press. (Filling the lubricator jar with light oil will assure long air cylinder life.)

The Parker valve allows manual selection of the shut, open, or "neutral" position. This valve connects air supply from the regulator to one end of the air cylinder, while simultaneously opening the other end to atmosphere. This vent line on the 4-way valve allows air to escape when pressure is switched from one end of the air cylinder to the other.

Continuous air flow from the Parker vent line indicates a leak inside the air cylinder, or possibly a faulty 4-way valve.

Once material is going through the press, set the 4-way valve so that the discharge cone goes shut in the "in" or closed position. Start with a low air pressure, working your way up until the desired performance is obtained.

The neutral position is used only in testing. If left in the neutral position, the cone will not move unless it is pushed open by press cake. If, later, the flow of press cake is diminished, the cone will remain in the position to which it was pushed.

AIR REGULATOR WITH REVERSING VALVE

DISCHARGE CONE
The principal adjustment of the press is made with the discharge cone. The cone is the component at the cake discharge end of the press that acts as a stopper plug to restrict material from leaving the press. The more pressure exerted by the discharge cone, the dryer the cake material will be leaving the press. Also, the motor amps can be expected to increase with added pressure.

In the small CP-4 press, the cone is usually actuated by either a weight arm or an air cylinder.

Presses are generally started up with the cone in the withdrawn position. Once material is going through the press, the cone is set to the closed position. With many materials it is satisfactory to start the press with the closed position. However, with materials that are dry to begin with, such as swarf or plastic wash tank sludge, it becomes more important to start with the cone in the open position in order to prevent an unnecessary jam. Also, very thin or soupy materials, like pumped pig manure or clarifier underflow, might tend to purge right through the press if the press is started with the cone in the open position; with these materials it is frequently better to start up with the cone nudged into the closed position.

As the pressure on the cone is increased, not only will the cake become drier, but the flow through the press may also be reduced. With very slimy inbound material it is sometimes possible to apply enough cone pressure to stop the flow altogether.

High cone pressures will result in increased quantities of suspended solids in the press liquor.

Typical air cylinder pressures to actuate the discharge cone are in the range of 30 to 60 psi. Some materials will press only in a low range, say 15 to 20 psi. Other materials may press best with a pressure of 60 to 100 psi. Air consumption is minimal in all models, 1 to 2 cfm.

On models without an air cylinder, typical weights used actuate the discharge cone vary considerably. When juicing fruit there may be a need to minimize the amount of solids being forced through the screen. At the other end of the scale, sometime applications require an extension arm with very heavy weight.

It is acceptable to open the discharge cone, in most cases, during normal operating conditions. This allows inspection, while in operation, of the discharge end of the screw and screen. This will give the operator a chance to observe operation with minimum dewatering and maximum throughput. It is also a good technique for purging bad material (i.e., either jammed or spoiled material) from the press. (Do not try this trick if you are pressing hot or chemically aggressive materials.)

With some feed materials, the press can be operated with the cone in the withdrawn position. The screw itself will do enough compressing and dewatering to produce a cake at the discharge. If the material being pressed dewaters very readily, the press can jam even with the cone in the withdrawn position. If this happens, a lower compression screw is called for.

An unusual technique is to set the air pressure so that the cone normally stays completely shut. A timer is used to periodically open the cone. The closed period is determined by the amount to time required for press cake to accumulate in the press. This type of operation is used with slippery or slimy press cake that cannot be dewatered to sufficient firmness to force the cone open. The duration of the "cone open" period is long enough to dump the press cake that has been formed. Cone Timer panels are available from Vincent at no charge.

It is undesirable to leave a press running at a very low pressure like 10 psi. Once some fiber enters between the cone bushing and the screw shaft, it will take more than that much pressure to close a cone has have been pushed open by a heavy flow of cake. The result will be either high moisture content in the cake or, worse, purging.

Where very low air pressures are required for proper operation, it may be practical to put the 4-way valve in a neutral position, half way between open and closed. (Keep in mind that a slug of cake will push the cone open, and it will not re-close on its own afterwards.)

Once through start-up, the cone is almost always permanently left in the closed position at whatever air pressure had been found to be effective. A plug of cake will be left around the cone whenever the press is turned off; this will clear on its own accord on restarting the press.

INTERMITTENT OPERATION
In the case of intermittent operation, the control panel for the feed pump or conveyor and the press should have a timer. This timer should be set to have the press run for three minutes after the feed pump (or conveyor) shuts off. This will partially clear the press so that it will not trip out on overload when it is re-started. (This applies in high torque applications or with installations where the material in the press dries out or freezes.)

An extreme case occurs when pressing spent coffee grounds and some paper mill fibers. Each time the press is turned off, the cone must first be opened for two minutes. If this precaution is not taken, severe damage to the press can occur when the press is re-started.

Minimize the time that the screw press is run with no material being fed into it. Since the screw is supported to some extent by the material inside the press, running dry may allow the screw to rub the screen. The last material admitted to the press will dry to powder, and, as such, it will not provide the lubrication required to prevent abrasive wear. (Initially the press will likely be run dry in order to check rotation; negligible wear will occur so long that this period is kept to a minimum.)

DOUBLE PRESSING
Some processes benefit from what is called double pressing. This means that the cake coming from the press is run through the press a second time, or through a second press. If little moisture is removed in the second (double) pressing, then it is known that the liquid removed in the first pressing is all of the free liquid that there is to be pressed out.

Sometimes water is added to the cake in between the first pressing and second pressing. This is done to enhance the recovery of dissolved sugars in the original press cake.

Molasses can be added to press cake between the first and second pressing. This is used to infuse dissolved sugar into the cake, reducing the final press cake moisture content.

Capital-effective double pressing can be achieved by using an inexpensive Soft Squeeze Series KP screw press for the first pressing, following with a tighter-pressing Series CP or VP in the second position.

MOISTURE CONTENT
A screw press separates free water. This will leave organic water in the press cake. The organic water is either bound to, or part of, the animal or vegetable molecules. Mechanical pressure alone will not remove organic water; it takes heat or chemistry. Frictional heat from the press can remove organic water, but this obviously should be avoided. For chemistry, see the Hydrated Lime, Gypsum and Alum section.

To determine the moisture content of a material (feed to the press, press cake, or press liquor), a sample should be weighed and dried overnight at a temperature slightly less than 100º C. The sample should weigh six or more times the tare weight of the sample tray or cup.

The moisture content of press cake varies considerably. Tomato press cake will be 90% moisture. Orange peel will be 80%, unless it is reacted with hydrated lime, in which case it will go down to 72% moisture; add molasses and it will go to 65%. Dairy and hog manure will come out at 70% moisture, unless there is sand or sawdust in the sample, which will reduce the moisture content. Cellulose fiber from a paper mill (knots, screen rejects, primary clarifier underflow) will come out about 50%. However, if secondary (biological) sludge is added, then the moisture content of the cake will go up considerably. Moisture contents of only 25% can be achieved pressing things like glass, sand, and plastic chips.

The heat from steam injection can change the chemistry of the material being pressed so that cake with lower moisture content is produced. This works with fish and orange peel, for example.

A quick approximation of what to expect from a screw press is to squeeze as much water out with your fist, and figure that the press will do a little bit better. Another way is to twist a ball of material in a cotton cloth.

COMPRESSION
A screw press achieves compression using several methods: (1) The discharge cone of the press causes back-pressure on the material being dewatered. The higher the cone pressure, the greater the liquid removal. (2) The pitch of the flights of the screw tightens as the material is conveyed through the press. This forces liquid to go through the screen. (3) The diameter of the shaft of the screw may be increased, forcing material outward, against the screen.

Force-feeding (supercharging) the press and applying a vacuum to the outside of the screen are two additional methods which may achieve compression. These two are used infrequently because the performance results are uncertain.

PRESS SPEED (RPM)
In general, the slower the screw speed, the greater the dewatering. Longer residence time in the screened area results from lower screw speed, which allows time for more thorough dewatering. Unfortunately, it also goes with reduced throughput capacity.

Screw press speed (rpm) can be changed by going to a different rpm drive motor (900, 1200, or 3600 versus the standard 1800 rpm). Alternatively, a Variable Frequency Drive (VFD) can be used. Most modern motors are good for permanent 120 Hertz operation; they are always good for a test at this high speed.

The Nord gearboxes are all rated for 4,000 rpm input, which makes it easy to switch to a 3600 rpm motor. It is best to switch to synthetic lubricant if this change is permanent. With other gearboxes, the higher speed can result in premature gearbox failure. Consult the factory for assistance.

A small change in screw speed, like 20%, will generally not result in a measurable change in performance of the press.

It is unusual for a variable speed drive to be used with a Vincent single-screw press, except when testing to determine optimum speed.

Low screw speeds are used for cooker crumb, potato peel, and many sludges.

CAPACITY MEASUREMENT
The best way to measure capacity of a press is to collect timed samples of press cake and of press liquor. This should be done during a period of sustained, stable operation, rather than by running a batch through the press.

Press cake is generally captured in a tarpaulin, and press liquor in a 5-gallon pail or 55-gallon drum. When the drain is at floor level, a 3-mil plastic bag can be used to catch press liquor.

If it is not possible to collect either press cake or press liquor, it is possible to calculate the press throughput if the inbound solids content and press cake solids content are known. It is assumed that there are zero suspended solids in the press liquor, although this is never the case.

A-B-C-D PLATES
There are four vertical plates making up the frame of the press. Starting from the drive end of the press, the first one is the Adaptor Plate. The gearbox is bolted to the adaptor plate. Through four spacers, the adaptor plate is welded to the A Plate. This A Plate forms one wall of the inlet hopper; the shaft seal housing is bolted to the A Plate.

The second plate is the B Plate. It forms the other wall of the inlet hopper. The screen starts at the B Plate. There is a part called a Stripper welded to the B plate, inside the inlet hopper, in a position to kiss the screw flight as it goes past. Also, there is a notch, called a Cord Cutter, in the B plate.

The final plate, the C Plate, supports the discharge end of the screen. The cone lightly touches the C Plate when in the closed position.

SCREW LIFE
If a press loses its previous throughput capacity, or if cake moisture content increases, it is a sign of a worn screw.

A screw can last anywhere from six months to twenty years. It depends on the material being pressed and how hard it is being pressed.

Premature screw failure can arise from several causes. The two main ones are:

If a press is allowed to run continuously even when no material is being fed into it, the screw can wear out in two or three months.

If abrasive material is dewatered with high cone air pressure, rapid wear will occur. This condition is avoided if a few drops of water can always be squeezed from a fistful of press cake.

Two effective ways to extend screw life are:

• Various grades of hardsurfacing rod can be used to protect the flights of a screw. Ultinium (Rockwell 90) is harder than most Colmonoy and Stellite alloys.
• Using a VFD or lower speed motor to reduce the screw rpm will extend screw life

If a worn screw is suspected, the thing to do is to shut down the press, open the cone, and dig out the cake until the tips of the last two flights can be seen. Check how badly the tips are worn. If the there is 3/8" between the tips and the screen, serious wear is evident. It is also an indication that the sharp edges of the flights throughout the press may have worn, becoming rounded. This can cause the flights to act like a putty knife, plastering solids against the screen, preventing water from coming through.

Worn screws are either restored locally or returned to Vincent for rebuilding. The cost of a screw rebuild is around one third the cost of a new screw.

SCREW CONFIGURATION
Almost all Vincent Screw Presses use the Interrupted Screw Flight design. The interruptions leave room for four stationary resistor teeth that are mounted outside of the screen. These teeth go through the screen and reach almost to the shaft of the screw. This design of screw press stands in contrast to a Continuous Screw design. The main advantage of the interrupted design is that solid material must accumulate in the interruptions until sufficient consistency is reached for the solids to be pushed toward the cake discharge. There is a reduced tendency of the material being pressed to co-rotate with the screw. Also, there is more agitation within the press and, consequently, quicker dewatering.

The screw starts with a feeder section of continuous flight. This picks up material in the inlet hopper and pushes it into the screen section. The feeder section ends at the first resistor tooth. The feeder section of the screw is followed by compression stages where the flights have reduced pitch. The reduction in pitch of the flights results in compression of the material going through the press. CP-4 presses are made with four stages of compression.

A screw configuration referred to as Sterile Butterfly is available. There are a reduced number of flights on this screw, and the flights do not wrap as far around the shaft as is normal. This design screw is good for high throughput of materials that are easily dewatered. Produce waste, dairy manure, and knots are typical examples. This configuration is rarely used in the CP-4 press.

INTERUPTED FLIGHTS AND RESISTOR BARS

PIE CUTTING
Sometimes the compression of a screw is reduced, in the field, in an operation called "pie cutting". This involves cutting pie-shaped segments from certain flights of the screw, leaving a butterfly (end view) configuration. It is useful in modifying a press so that excessive compression and jamming are avoided. The "sterile cut" is more dramatic. Consult the factory for assistance before making this modification.

4" PIE CUT	PIE CUT	NOT PIE CUT

JAMMING
Should a press become jammed a series of steps can be taken to un-jam the press. Generally the easiest thing to do is to reverse the direction of rotation. This will cause the screw to feed material backward into the inlet hopper.

Generally jamming is caused by over-pressing excessively dry material. Running the press backwards will break up this material. If the jamming was caused by tramp material, hopefully this can be found and retrieved from the inlet hopper following operation in the reverse direction.

If a press has had extensive use in an abrasive application, the flights can be worn away at the discharge of the press. Radial wear of 1" to 4" will lead to serious jamming and, possibly, a burst screen.

When a press is operated in the reverse direction it is possible that solid material in the press will be forced against the A Plate. This can damage the Shaft Seal. For this reason, care should be taken when running the press backwards.

If running the press backwards does not clear the jam, the screen should be removed so that the cause of the jam can be determined. Look for a bent flight. Before going to the trouble of removing the screen, shut down the press and try clearing the end of the press with a long screwdriver.

SCREEN BLINDING
A common problem is for the screen of the press to become blinded (covered over). When this occurs, the flow of press liquor coming through the screen diminishes.

In some cases, the screen can be cleared by periodically reversing the direction of rotation of the screw. This can be programmed with many VFD's, so that the press runs forward for a given period and then reverses direction briefly when the screen starts to blind. This is one of the easiest possible solutions to test. Sometimes it is the only one that is effective.

Many other methods are used to address blinding: (1) Adding notches to the screw, (2) Reducing or eliminating the pressure in the inlet hopper, (3) Adding press aid to the flow, (4) Changing to a different screen selection, (5) Reducing the screw-to-screen clearance, and/or (6) Employing a back-flush with caustic solution, acid, or high pressure spray.

If blinding occurs after an extended period of satisfactory operation, it is usually due to wear of the screw. Rounded edges of the flights will contribute to blinding.

CHANNELING
A condition somewhat similar to purging can occur with slimy materials, like concord grapes, pineapple pulp, or spent brewer's grain. These may tend to channel or squirt out of one side of the cone. Two ways to eliminate channeling are to lower the pressure on the discharge cone, and to slow down the speed of the press. Channeling can also be reduced by adding press aid to the material being dewatered, or by reducing the inbound flow to the press.

An option NOT available with the CP-4 press is called the Rotating Cone. A tendency for material to channel can be reduced with this option. The cone is caused to rotate so that the relative motion between it and the (stationary) main screens breaks the channeling. (If there is a hole through the shaft of the screw near the cone, put a bolt through this hole.)

To break up channeling, pieces called wing feeders can be welded to the end tips of the last two flights of the screw. See the Wing Feeder section of this manual.

PURGING
An undesirable condition can occur when the material being admitted to the press purges, without liquid-solid separation, from the cake discharge. This can occur especially if pressure exists in the inlet hopper.

Mechanically, purging occurs when a dry lump of press cake holds open the discharge cone. Un-pressed material will flow around this partial plug.

Purging may occur when there is a much reduced, small flow of cake coming from the press. Usually this is a sign of a blinded (covered over) screen. Frequently this is caused by a worn screw. Liquid from the inlet hopper will wick into the press cake, making it soft enough to blow out. Mount the press inclined at about 5º above horizontal to help avoid this condition; the simplest way to do this is to place a block under the cone end of the press.

Wing Feeders can be welded to the tips of the last two flights of the screw in order to break up dry cake which is holding the cone open.

Purging is prevented with the rotating cone option. This option is very unusual in the Series CP presses, and it may not be available. However, if there is a hole through the shaft of the screw near the cone, put a bolt through this hole.

A drop in operating amps is frequently an indicator that a purging condition has begun. An ammeter circuit can be installed to trip the system when a reduction in motor amps occurs. This is rarely done.

BRIDGING
Sometimes bridging will occur in the inlet hopper, stopping the flow of material into the press. Poking with a broom stick is the easiest way to solve this during a simple test. A more permanent way to overcome bridging is to direct a stream of water into the inlet hopper so as to break the bridge. The nature of the screw press is that essentially all of this added liquid will be removed in the pressing operation.

If a surge hopper is mounted over the inlet to the press, it should have at least one, preferably two or three, vertical walls. This will minimize bridging.

Bonding Teflon sheets to the inlet hopper of the press is a remedy that has been used to reduce bridging of bulky materials which allow free-draining of water.

A vibrator, mounted on the side of the inlet hopper, may also alleviate bridging.

AUTO-REVERSING VFD
Some applications require the use of a specially programmed variable frequency drive (VFD). In this case the VFD is not necessarily used to change the speed of the press, but, rather to set it for auto-reversing operation. By having the press run backwards for two or three turns every 30 seconds or so, many difficult-to-dewater materials can be pressed much more effectively. This operation is indispensable for tomato waste, and it helps a great deal with any other material that tends to blind (cover over) the openings in the screen. Vincent has loaner VFD's if you want to give it a try.

RESISTOR TEETH
The interrupted screw design press has stationary teeth that protrude into the flow of material as it passes through the press. These fit into the gaps of the screw where there is no flighting. They stop just short of the shaft of the screw.

Rarely the resistor teeth are shortened, usually by half, to increase the capacity of the press. Removing the teeth altogether will result in co-rotation and jamming.

FLUID INJECTION
Resistor teeth can be drilled so to permit injection of steam, solvent or wash water while the press is in operation. Also, these modified resistor teeth can be used for in-place CIP cleaning, without the need of removing the screen from the press.

Injection is achieved by drilling holes through the resistor teeth, and piping these holes to a manifold outside of the screen. This arrangement is used in dewatering raw, slimy organic materials, as well as in pressing materials that need to be washed as they go through the press. Photos and drawings are available from the factory. Steam injection works well on pineapple skin, citrus waste, and raw fish.

The moisture reduction that results from steam injection is related to a chemical change that comes with blanching, or parboiling, a material. Tests run with steam injection in a Vincent press at Anheuser-Busch showed little benefit. The material being pressed, spent grain, had already been "cooked" before steam was added.

Photos and drawings are available from the factory. Vincent does not charge for providing a drilled resistor bar.

STEAM INJECTION IN TWIN SCREW PRESS	LAB PRESS STEAM INJECTION

CORD CUTTER AND STRIPPER
Sometimes long stringy material will be pinched where the feeder portion of the screw goes through the hole in the B Plate. This material will co-rotate with the screw and build into a bundle which reduces the flow through the press.

A groove, like a keyway that is 3/8" deep, is cut through the hole in the B plate. We call this a Cord Cutter. Material trapped between the flight and the hole in the B plate will pop up slightly as it passes the Cord Cutter. The result is that the material is sheared loose.

A part called a "Stripper" is welded to the B Plate, inside the inlet hopper. It is welded in a position so that the flight lightly kisses the stripper as it goes past. This strips the material away. Strippers are made of key stock.

CORD CUTTER	STRIPPER AND CORD CUTTER

VACUUM EFFECT
In some applications, increased screw press capacity can be obtained if the area outside of the screen is under a vacuum. This can be achieved by mounting the press at a high elevation, with the press liquor drain line dropping below the surface of a drain tank or pit.

That is, the drain line from the press should go below the surface of the pit or pond into which it drains. If this line is relatively small in diameter and has a steady downward slope, a vacuum will be induced around the screen of the screw press. The mass and velocity of press liquor flowing through the drain line create this vacuum. To draw air bubbles downwards with the press liquor, the velocity of the fluid must be greater than five feet per second.

The cover over the screen of the press will have to be sealed, usually with Silicone.

The amount of vacuum is a function of the elevation between the press and the drain pond. For good results, the press should be mounted on a stand that is 20' or higher.

POLYMER
In rare applications, the addition of polymer is indispensable in achieving adequate screw press performance. Polymers are added to dilute waste streams, especially to those containing very small size suspended solids. The long chain molecules of the polymer will flocculate the solids, agglomerating them to the point where they can be pressed. Under the right conditions, drastic improvement can be observed in press throughput, press cake moisture, and pressate clarity.

Nalco and GE are the leading polymer suppliers. They can recommend the product best suited for your application.

Low speed operation of the press is usually required in order to achieve good performance.

Sometimes polymer addition tends to blind (cover over) the openings in the screen. In such situations, the press will work only if no polymer is used.

NOTCHES
Sometimes it is necessary, during press operation, to have the screw wipe the screen clear of blinding material. Cutting shallow notches (1/8" wide by 1/8" deep, 1" apart) in the outer edge of the screw flights best achieves this. Typically, notching is done from the B plate to the second resistor tooth. Fibrous material accumulates in the notches and wipes away slimy material which may be blinding the screen.

GRINDING NOTCHES IN THE FLIGHTS

WIPERS
Before the advent of notches, wipers, made of UHMW strips or nylon brushes, were (rarely) mounted to the outer perimeter of the screw flights. If at all possible we advise against the use of such wipers because (a) they tend to cause material to co-rotate and jam in the press, (b) they are difficult to replace, and (c) they wear rapidly, resulting in unacceptably frequent shutdowns for replacement. Wipers tend to improve dewatering performance for the first week or so. After that the wiper material wears and press performance reverts to being just a little better than if no wipers were used. Wipers are made either of 1/4" thick high durometer polyurethane or of nylon bristle brush. Wipers are preferably mounted on the downstream edge of the flight.

PRESS AID
Some materials press best if a press aid is mixed into the material to be pressed. Typical press aids are rice hulls, cottonseed hulls, cellulose fiber from a paper mill, and ground newspaper.

Press aids are most commonly used in producing juice from deciduous fruit. The press aid gives the press something to get a bite on. Press aids also tend to hold back suspended solids (short fibers) and prevent them from going through the screen with the press liquor. If apples are fed into a press, apple sauce will come through the screen. However, if a press aid is added to the apples, then apple juice will come through the screen.

Typically, the amount of press aid used is only 1% to 3% by weight of the flow going through the press. This will look like more than such a small percentage because press aids have a much lower bulk density than the wet materials that are pressed.

HYDRATED LIME, GYPSUM, AND ALUM
Lime (calcium hydroxide) must be added to citrus peel before it can be pressed effectively. The lime breaks down the pectins or cell walls so that the press can remove moisture. Less than 1% by weight is used. A reaction time of several minutes must be allowed prior to pressing. Lime has been used successfully in the same manner with potato, onion, tomato, carrot, and pineapple waste. It works well on acidic materials such as onions, strawberries, and coffee bean pulp. Vincent offers liming systems.

Gypsum and alum salts are also effective chemical press aids. They are typically used in dewatering sugar beet pulp, and they have been found effective on other materials.

PRESS LIQUOR
A Screw Press produces relatively "dirty" press liquor as compared to a Filter Press. Suspended solids will pass through the screen of the screw press along with the liquid being expressed from the inbound material.

If suspended solids need to be removed from the press liquor, the most common method is to pump the press liquor either over a static (sidehill) screen or through a rotary drum screen. Generally, the screen tailings (sludge solids) are fed back into the screw press along with the flow of inbound material. Most of these solids will be captured with the solids of the inbound material and end up in the press cake. Although some of these tailings will once again go through the press screen with the press liquor, equilibrium is reached and stable pressing operation is realized.

If the press liquor is to be concentrated in an evaporator, better screening than can be achieved with a static screen may be required. Another Vincent machine, the Fiber Filter, provides premium performance. Decanters and centrifuges may be required.

SCREEN SELECTION
The screen of the CP-4 press is made of slotted wedgewire. Wedgewire screens are one piece weldments that must be replaced when excessive wear has occurred. The standard screen used in the CP-4 has a slot width of .015" to .020". With the advent of recovering cooking oil from cooking crumb, a 0.008" screen has been introduced.

The most common damage to a wedgewire screen is for part of the surface to be smeared over by rubbing the screw. This rarely is bad enough to affect press performance.

In the case where a few slots get spread apart by tramp material, TIG welding is used to close the gaps.

In cases of severe wear or damage, it is common to patch a screen. Stainless sheetmetal is used for this. The reduction in drainage surface is of little consequence as the screens have ample open area.

Perforated stainless steel sheet screens are rarely available for the CP-4 press. In other Vincent presses, perforated screens with hole sizes ranging from .020" to .095" are common. Surprisingly, there is little difference in the degree of filtration achieved by changing hole size. Where the holes are smaller than .050", the screen material is so thin that a reinforcing back-up layer of thicker screen is employed. This back-up material generally has 3/8" holes.

PROFILE BAR (WEDGEWIRE) SCREEN

PERFORATED SCREEN WITH REINFORING SHEET

SCREW-TO-SCREEN CLEARANCE
Generally the clearance between the screw and the screen is 1/32", plus or minus 1/32". The screw should not rub the screen hard, as it can cause wear and premature failure of the screen. Reduced clearance is used with materials that blind the screen, such as onion skins. With a clearance greater than 3/16", the dewatering performance of the press can start to deteriorate; this depends a lot on the type of material being dewatered.

With wedgewire screens, a feeler gauge can be slipped through and along a slot until it hits the edge of the screw. Measure from the outside of the screen to the edge of the flight; then subtract the thickness of the wedgewire (0.156") from the measured depth in order to calculate the clearance.

If a screw rubs against the screen in a given area, it may be best to grind some off the OD of the screw. Prussian Blue can be useful in finding the spot that is rubbing.

CONE BUSHINGS
The cone, which rides on the shaft of the screw, is made of bronze or UHMW to protect the journal surface of the screw shaft. Normally the journal area is lubricated with liquid from the material being pressed, such as the juice from apples.

The grease fitting is provided to minimize leakage of press liquor through the cone. It is also used for lubricating when materials that are quite dry (paper mill screen rejects) are being pressed. By the time such materials reach the discharge of the press, they do not have enough free moisture left in them to adequately lubricate the cone journal.

Automatic grease systems are available. These should be the high pressure electric or battery variety. Vincent provides these for critical applications, such as pulp & paper and alcohol extraction.

WING FEEDERS
Very rarely in the CP-4 press, there are blades welded to the outside tips of the last two flights of the screw. Called "Wing Feeders", these are mounted parallel to the discharge screen surface. Care must be taken that wing feeders are not made so long that they hit the face of the cone when the cone is in the closed position.

Wing feeders can serve three purposes. (1) In the case of materials that want to channel out the discharge of the press, like pineapple and spent brewer's grains, the wing feeders break up the channeling flow. (2) For abrasive applications, short knobby wing feeders are provided as sacrificial wear elements. (3) In the case of press cake that is very hard and which tends to jam at the discharge, the wing feeders can break up the cake to encourage a discharge flow.

Clumps of dry material can accumulate, especially in the CP-4 press, between a wing feeder and the shaft of the screw. This in turn reduces screw press capacity. Should the problem occur, either grind off or at least shorten the wing feeders by half.

Dry material can also pack between a wing feeder and the screen. This will wear out the screen in the area where the wing feeders are located. Removal of the wing feeders is recommended.

In abrasive applications, the thickness of the flights at the discharge should be monitored. When the flights wear very thin, it is easy for the wing feeders to break loose.

LONG WING FEEDER	KNOBBY WING FEEDER

CLEANING
Commonly material is cleared from a press by stopping the inbound flow, setting the cone in the withdrawn position, and running the press for several minutes until no further material is discharged. This will leave some material inside the press, which can be handy for forming a plug at the cake discharge when the press is restarted.

Material will leave a Vincent interrupted flight press only if there is additional inbound material forcing it out. This makes it difficult to clear all material from a press without removing the screen. One technique used successfully is to feed crushed ice into the press. Water must be fed along with the ice to prevent jamming. When the ice melts, the press will be relatively clean inside.

There are applications in which the press must be cleaned frequently, such as once a shift, in order to meet sanitary regulations. At these installations, the screen is removed from the press in order to remove residual material. In this situation a spare screen may be kept on hand in order to minimize downtime.

Cleaning the inside of the screen can be achieved by injecting water through the resistor teeth. Holes must be drilled in the resistor teeth to make this possible.

In laboratory applications, the press may be disassembled for cleaning. The various components can be dipped in an appropriate solution or placed in an autoclave.

There is a U-Tube video on the Vincent web site showing disassembly of the CP-4 press.

It is rare that the outside of the screen needs to be cleaned. A pressure washer or swabbing with acid solution can be used.

SHAFT SEAL
The Seal Plate is bolted to the A Plate. This plate may be solid UHMW (ultra high molecular weight polypropylene or polyethylene) or it may contain one or two Johns Manville (JM Clipper) lip shaft seals. There may be a grease fitting on this plate; the grease is used to reduce leakage and to help prevent trash material from entering the seal and damaging the screw shaft.

Generally, seals are allowed to drip once they start leaking. They are replaced only in conjunction with major maintenance, as when the screw is removed from the press.

In some cases we have found that leakage from a shaft seal can be stopped by simply selectively loosening or tightening the four bolts holding the seal housing to the A plate.

SEAL PLATE	SPLIT SEAL PLATE

SCREW REMOVAL
The screw is removed through the hole in the C Plate, at the cake discharge end of the press. The operation can be difficult the first time, so we recommend consulting with the factory before getting started.

First of all, remove the four bolts holding the shaft seal housing to the A Plate. This will prevent damage when the screw drops out of the gearbox.

The bar with the resistor teeth must be removed before the screw can be removed.

Series CP screw presses use a key and keyway to couple the screw inside the hollow bore of the gearbox. It may be that a great deal of force will be required to push the screw from the gearbox.

The basic procedure is to push or pull the screw out of the gearbox. If the screw is not tight, the screw is removed easiest by pulling, or by prying with a pry bar.

If it is tight, the screw is removed using a heavy fine-threaded rod to push the screw out of the gearbox. This rod is threaded through a heavy nut Vincent has provided inside the hollow bore of the gearbox. This nut has a lug that fits in the keyway, to prevent the nut from turning. The nut backs up against an internal snap ring in the hollow bore of the gearbox. The result is that the rod pushes against the end of the screw. Liberal use of Anti Seize or Never Seize is absolutely required to protect the threads. Loaner tool kits are available in Tampa; see Screw Change Kit Drawing B-94693.

Alternatively, the screw can be removed by constructing a gear puller, allowing the use of a hydraulic cylinder, combined with a cross bar and two long shafts threaded into the gearbox housing. The holes in the gearbox have metric threads. To avoid the need for metric all-thread rod, a length of all-thread rod with English threads is welded to the head of a metric bolt.

If the press has been badly jammed, the key may have rolled inside its pocket. In these cases it can be impossible to press the screw from the gearbox. It then becomes necessary to cut the screw in half, between the gearbox mounting plate and the A plate. The stub shaft can then be bored out in a large boring mill, and the screw can be repaired at the Vincent factory.

JACKING ROD

SCREW REPLACEMENT
In the case of the Series VP presses, jacking bolts and shims are used to achieve proper alignment. Only after the screw is aligned within the screen can the gearbox be aligned to the screw (not the other way around). When working with gear-type couplings, be sure to leave the prescribed gap between the gearbox shaft and the screw shaft. This will protect the gearbox from thrust loads.

Falk gear couplings must be heated to 350º F in order to slip onto the shaft.

There are two ways to avoid excessive rubbing between a new screw and the screen: Either shims can be placed between the screen frames and the resistor bars, or the interference can be ground off the edge of the screw. To eliminate the high spots, coat the edge of the screw with Prussian Blue, bolt the screens in place, turn the screw, remove the screens, and grind the screw where interference has occurred.

SCREEN REPLACEMENT
When reinstalling a screw, the screw must be pushed in until the step in the shaft seats against the thrust bearing of the gearbox. This will position the flights of the screw so as not to be hit by the resistor teeth. Be careful when guiding this step in the shaft through the shaft seals.

During re-assembly of a keyed shaft, be sure to apply Never Seize or Anti Seize to the portion of the screw shaft that goes into the gearbox.

When installing a screw into the press, it may be necessary to use a long allthread rod (English threads). This rod is screwed into the threaded hole on the end of the screw. The screw is slid into the press far enough that the allthread rod goes through the hollow bore of the gearbox. A large washer is slid along the allthread rod to form a brace against the gearbox. Running a nut on the rod, against this large washer, will pull the screw into the gearbox.

Excessive rubbing between a screw and the screen can be corrected by grinding the high spots of interference off the edge of the screw. Prussian Blue, applied to either the screw or the screen, can be useful.

GEARBOX BASICS
Model CP-4 presses use Nord hollow-shaft gearboxes, with C-face mounted motors.

Gearboxes are rated, and sold, by torque. The manufacturers generally offer their designs in progressively larger sized castings, or boxes. The larger the box, the larger the torque rating. Each box size will be available with different gear ratios. In order to keep the torque fairly constant, larger horsepower motors are used with the high speed boxes. Similarly, smaller horsepower motors must be used when a low output speed is selected.

Sometimes screw presses are designed around the size of the gearbox that is selected.

REPLACEMENT PARTS
Most replacement parts are standard OEM components which are be purchased from their original manufacturer. The specification of these items (gearbox, seals, air cylinder, etc.) is included in the O&M Manual.

The most common wear parts in the Vincent CP-4 Press are the screen, the screw , the cone, and the outboard support bushing. Vincent stocks these. Screws are generally rebuilt at the Vincent factory. Be sure to specify the Serial Number of your press when ordering replacement parts or repairs. If work is required on the screw, it may be more convenient to obtain a loaner press and return your machine to the factory.

SAFETY
These Operating Hints have left unstated the obvious safety hazard: A screw press, like any screw conveyor, is totally unforgiving. If clothing or a limb gets caught in a rotating screw, the screw will not stop. Vincent Corporation has heard of only one injury of this nature with a screw press; do not let yourself become the second. The use of common sense is all that is required.