This specification relates to separating solids from liquids, screw presses and to methods of thickening sludge.
In general, a typical screw press comprises a screw, also called an auger, rotating within a fixed cylindrical body comprising screen panels. A solid-liquid mixture to be treated is fed into an inlet end of the screw press. The auger conveys the mixture through the cylindrical body while pressing the mixture against the screens. Liquid and fine solids are collected from the outside of the screens. Retained solids and residual liquid are collected from an outlet end of the screw press. The cylindrical body is dismantled when the screens need to be cleaned.
In International Publication Number WO02/062564, a screw press is used to separate solids from sewage. A screw is driven by an electric motor. The direction of rotation of the screw is reversed periodically to clean the screw press.
In International Publication Number WO99/52704, a screw press has a cylindrical body made up of a stack of annular plates. Some of the plates are fixed and some of the plates are movable. An eccentric shaft passing through the stack of plates rotates when the auger rotates. The rotation of the eccentric shaft causes the movable plates to oscillate relative to the fixed plates.
The following introduction is intended to introduce the reader to the detailed description but not to limit or define the claimed invention.
A screw press described in this specification has a cylindrical screening section mounted to a frame of the press such that the screening section is able to rotate. Restraints between the screening body and the frame may be configured to allow the screening body to rotate or to inhibit or prevent the screening body from rotating. A sprayer system is provided on the outside of the screening body. A motor may be used to cause the screening body to rotate. Optionally, the motor may also drive an auger within the screening body.
A screw press described in this specification has a screening body with opening sizes appropriate to retain flocculated solids. Optionally, a sprayer system may be provided on the outside of the screening body. Optionally, an auger shaft may have an increased diameter towards an outlet end of the press.
A screw press cleaning method described in this specification comprises steps of spraying water at a screening section of the screw press from outside of the screening section. Optionally, the screening section may be rotated while water is sprayed at it.
The invention provides an alternative device for separating solids from a liquid or an alternative method of operating a screening device. The device and method may be used, for example, to thicken sludge from a wastewater treatment plant such as primary or activated sludge from a municipal sewage treatment plant.
The screw press 10 also has an auger 14 and a drive mechanism 18. The auger 14 is located within the screening body 12 and is supported by the frame 16. In particular, the auger 14 and screening body 12 are concentric about a central axis 32 of the screw press 10. One end of a shaft 60 of the auger 14 is supported through a bearing (not shown) on a stationary post 34 attached to the outlet portion 30 of the frame 16. The other end of the auger shaft 60 of the auger 14 is supported on a drive shaft 36 of the drive mechanism 18. A blade 58 of the auger 14 is attached in a spiral around the auger shaft 60 and extends towards, or optionally touches, the inside of the screening body 12. The drive mechanism 18 is attached to the inlet portion 26 of the frame 16 and comprises a motor 38 and a gearbox 40. The frame 16 is supported on the ground through a frame 41.
The inlet portion 26 of the frame 16 has an inlet 42 to receive a feed mixture 44. The central portion 28 of the frame 16 has a liquid outlet 46 to discharge a liquid fraction 48 of the feed mixture 44. The outlet portion 30 of the frame 16 has a solids outlet 50 to discharge a solids fraction 52 of the feed mixture. The liquid fraction 48 may have some solids remaining in it but at a reduced solids concentration relative to the feed mixture 44. The solids fraction 52 may have some liquid in it but at a higher solids concentration than the feed mixture 44.
In operation, the feed mixture 44 is pumped into the inlet 42 at an initial pressure. The drive mechanism 18 rotates the auger 14 causing the blade 58 to convey the feed mixture 44 along the screening body 12. The auger 14 preferably also increases the pressure of the feed mixture 44. Liquid and fine solids in the feed mixture 44 are forced through the screening body 12. These liquids and fine solids are collected in the central portion 28 of the frame 16 and discharged through liquid outlet 46. The remainder of the feed mixture 44 exits the screening body 12 after passing by a counter pressure cone 60. Counter pressure cone 60 is biased towards the screening body 12 by a biasing mechanism 62 such as a set of springs or a pneumatic cylinder. The solids fraction 52 drops from the end of the screening body 12 and is discharged from the frame 16 through the solids outlet 50.
The internal volume of the screening section 22 preferably decreases towards the outlet end 8 of the screw press 10. This helps maintain pressure in the screening section 22 even though the liquids fraction 48 is removed from the feed mixture 44. A decreasing volume may be obtained by reducing the diameter of the screening section 22. Alternatively, the pitch of the blades 58 may be decreased towards the outlet end 8 of the screw press. Both of these methods, however, prevent the use of a blade 58 having a uniform outer diameter and pitch, which is more easily manufactured to a tight fit with the screening section 22. In the screw press 10 of
The screening section 22 of the screening body 12 has openings of a size and shape adapted to provide a selected degree of separation. For example, the screening section 22 may remove fibrous materials from the digestate of an anaerobic digester treating manure or other agricultural wastes. Alternatively, the screening section 12 may have smaller openings suited to separating flocculated solids from primary or activated wastewater treatment sludge. For example, the screening section 22 may be made from wedgewire with a slot opening in the range from about 0.25 mm to about 0.75 mm.
Although any screw press may benefit from having a convenient cleaning method, cleaning is required more frequently when the screening section 22 has small openings. In particular, when the screw press 10 is used to thicken sludge, dismantling the screw press 10 for cleaning is undesirable. The screw press 10 is fitted with a sprayer system 70 to allow cleaning by spraying water against the outside of the screening section 22. When cleaning is required, water is pumped through a manifold 72 to a series of sprayer heads 74 located inside of the central portion 28 of the frame 16. The screw press 10 of
The water sprayed against the screening section 22 moistens and breaks up accumulations of solids caught in the openings of the screening section. Some of the water may also force its way through the openings of the screening section 22 in a reverse direction. The water is preferably heated. In order to assist the water in cleaning the screening section 22, the supply of feed mixture 44 may be stopped while the auger 14 continues to rotate for a period of time before the water is sprayed. This reduces the volume or pressure, or both, of the feed mixture 44 inside the screening section 22.
Referring to
Referring back to
Referring back to
An alternative mechanism for supporting or facilitating a desired rotation of the screening section 22 is shown at the top of
When rotation of the screening section 22 is not restrained, the screening section 22 will tend to rotated with the auger 14 due to friction between the auger 14 and the screening section 22. Optionally, the screening section 22 may be forced to rotate with the auger 14 by actuating a releasable connection (not shown) between the auger 14 and the screening section 22. Alternatively, the screening section 22 may be driven by the drive mechanism 18 without applying force through the auger 14, for example by use of the gear shaft 110 of
The screening section 22 is preferably rotated while water is sprayed against it during the cleaning process described above. Rotating the screening section 22 allows each part of the screening section to pass under a line of sprayer heads 74. Multiple manifolds 72 are not required. Rotating the screening section 22 also allows each part of the screening section 22 to be placed at or near the top of the screening section 22 so that gravity may assist in the cleaning. Rotating the screening section 22 also avoids having the bottom of the screening section 22 accumulate solids that fall from upper parts of the screening section 22 during cleaning. Optionally, the screening section 22 may be stopped and the auger 14 may be rotated for a period of time during or after the cleaning procedure to convey backwashed solids out of the screening section 22. Alternatively, the auger 14 may be rotated at a faster speed than the screening section 22 during the cleaning process to convey material released during cleaning out of the screening section 22.
After the cleaning procedure, the screening section 22 is restrained from rotating, the auger 14 resumes or continues normal rotation, and the supply of feed mixture 44 is restarted. The screening section 22 is typically prevented from rotating during operation of the filter press 10 except when cleaning the screening section 22.
This application claims the benefit of U.S. Provisional Application No. 61/636,000 filed Apr. 20, 2012, which is hereby incorporated by reference.
Number | Name | Date | Kind |
---|---|---|---|
1564585 | Krause | Dec 1925 | A |
2634776 | Kowan | Apr 1953 | A |
4286512 | Berggren | Sep 1981 | A |
6395187 | Alanis | May 2002 | B1 |
6651822 | Alanis | Nov 2003 | B2 |
6899807 | Cummings | May 2005 | B2 |
8017021 | Staples | Sep 2011 | B1 |
8302780 | Mitchell et al. | Nov 2012 | B1 |
20030042193 | Alanis | Mar 2003 | A1 |
20130213904 | Mitchell et al. | Aug 2013 | A1 |
20130277319 | Theodoulou | Oct 2013 | A1 |
20150076059 | Theodoulou | Mar 2015 | A1 |
20150076085 | Theodoulou | Mar 2015 | A1 |
20150329399 | Kumar | Nov 2015 | A1 |
Number | Date | Country |
---|---|---|
HO4200899 | Jul 1992 | JP |
HO6098513 | Dec 1994 | JP |
2005279731 | Oct 2005 | JP |
HO6098517 | Jul 2013 | JP |
Entry |
---|
English Abstract of JP 2005279731. |
English Abstract of JP HO4200899. |
English Abstract of JP HO6098513. |
English Abstract of JP HO6098517. |
International Search Report of PCT/CA2013/050297. |
Number | Date | Country | |
---|---|---|---|
20130277319 A1 | Oct 2013 | US |
Number | Date | Country | |
---|---|---|---|
61636000 | Apr 2012 | US |