Filtering device for removing impurities in a mixture of biological diatomite

Information

  • Patent Grant
  • 11260325
  • Patent Number
    11,260,325
  • Date Filed
    Thursday, August 13, 2020
    4 years ago
  • Date Issued
    Tuesday, March 1, 2022
    2 years ago
Abstract
The present invention discloses a filtering device used for removing impurities in a mixture of biological diatomite, which relates to the technical field of sewage treatment. This device includes a plurality of deflectors evenly distributed in multiple layers in the vertical direction. Each deflector includes a shell and a top plate. There is a filter unit symmetrically arranged on the left and right sides of each deflector. The top of the shell is covered with a top plate hinged with the depressed plate. The bottom of the shell is provided with water inlets which communicate with the shunt pipe, and the upper parts of the left and right side walls of the shell are provided with overflow ports. The shell also has a plurality of diversion folding plates located below the overflow ports and vertically staggered and distributed on the left and right side walls. The filter unit includes an inclined water guiding groove and a filtering plate.
Description
CROSS REFERENCES TO THE RELATED APPLICATIONS

This application is based upon and claims priority to Chinese Patent Application No. 202010008273.6, filed on Jan. 6, 2020, the entire contents of which are incorporated herein by reference.


TECHNICAL FIELD

The present invention relates to the field of sewage filtration and treatment, and more particularly to a filtering device for removing impurities in a mixture of biological diatomite.


BACKGROUND

The biological diatomite mixture is a mixture with high sludge concentration, proper viscosity and slower flow rate than normal sewage. The traditional filtering device for removing impurities in the biological diatomite mixture is generally a single-layer screen or bar. After the biological diatomite mixture passes through a single-layer screen or a bar, the particles and impurities in the mixture with the particle size larger than the mesh size of the screen or the bar are retained.


Due to the limited daily treatment capacity of the single-layer screen, the filtration efficiency of the traditional filtration device for the biological diatomite mixture is relatively low. If the sewage treatment capacity is large, then a large floor area is required to increase the area of the parallel screen. In addition, there are many fine particles in the biological diatomite mixture. When the traditional filtration device is used to treat the biological diatomite mixture, the filter plate is likely to be partially blocked, resulting in no sewage flow or a slow flow speed in part of the gap, which reduces the flow area of the filter plate and the filtration efficiency. Moreover, the traditional filtration device cannot selectively intercept the particles with different particle sizes. When the sewage containing the impurities with different particle sizes passes through the filter plate with the same gap, it is prone to the blockage of the filter plate, thus further reducing the filtration efficiency of the filtration device.


SUMMARY

In view of the above technical problems, the present invention provides a filtering device for removing impurities in a mixture of biological diatomite. The filtering device has a simple structure. By spatially stacking multiple layers of filter plate units and setting the filter plates into inclined curved filter plates, the problem of clogging that easily occurs in the filter plates can be alleviated which saves space, and can greatly improve the filtration efficiency of diatomite mixed solution. By installing a deflector and a depressed plate, the water distribution can be made more uniform, thereby alleviating the accumulation of the diatomite mixture unevenly distributed on the filter plate due to uneven water distribution, which can further avoid the clogging of the filter plate and improve the filtration efficiency of the filtering device.


To achieve the above technical objectives, the technical solutions of the present invention are as follows.


A filtering device for removing impurities in a mixture of biological diatomite includes a water inlet pipe, a shunt pipe, a plurality of deflectors, a filter unit and a water collecting pipe. The plurality of deflectors are evenly distributed in multiple layers in the vertical direction. Each deflector includes a shell and a top plate, and the left and right sides of each deflector are symmetrically provided with a filter unit. The shell is provided with the top plate, and the top plate is hinged with the depressed plate through a hinge. The bottom of the shell is provided with a water inlet. The water inlet is communicated with the shunt pipe. A water distribution valve is provided on the shunt pipe, and overflow ports are provided on the upper left and right side walls of the shell. A plurality of diversion folding plates are horizontally arranged under the overflow port, and the plurality of diversion folding plates are staggered and distributed on the left and right side walls of the shell in the vertical direction.


The filter unit includes a water guide groove and a filter plate. The water guide groove and the filter plate are fixedly connected to the side wall of the shell. The water guide groove is arranged obliquely relative to the side wall. A water collecting space with a top opening is formed between the water guide groove and the side wall of the shell. A water collecting port is arranged on a front groove wall of the water guide groove, and the water collecting port is connected to the water collecting pipe. The filter plate is obliquely arranged in the water collecting space. The top of the filter plate is flush with the bottom of the overflow port, and the bottom of the filter plate is flush with the top of the right groove wall of the water guide groove. The water inlet pipe is communicated with each shunt pipe. A water outlet pipe is connected to the water collecting pipe, and the water outlet pipe is provided with a water outlet valve.


The filtering device has a simple structure. By spatially stacking multiple layers of filter plate units and setting the filter plates into inclined curved filter plates, the problem of clogging that easily occurs in the filter plates can be alleviated, which saves space and improves the filtration efficiency of diatomite mixed solution. By installing a deflector and a depressed plate, the water distribution can be made more uniform, thereby alleviating the accumulation of the diatomite mixture unevenly distributed on the filter plate due to uneven water distribution, which can further avoid clogging of the filter plate and improve filtration efficiency.


Preferably, the bottom of the water guide groove is a curved surface. In this way, the volume of the collecting space of the water guide groove is increased. The water filtered by the filter plate is readily diverted to the water guide groove.


Preferably, the filter plate is an arc-shaped mesh plate curved toward the water collecting space. In this way, the filtering area of the filter plate can be increased, and the filtering efficiency of the device can be improved, which is conducive to guiding the water filtered by the filter plate into the water guide groove.


Preferably, the filter plate is a screen with a clearance of 0.5-5 mm grid or mesh no less than 50 meshes.


Preferably, the bottom of the filter plate is smoothly connected to a slag guide plate.


Preferably, the filter unit also includes an upper shutter for covering. The upper shutter includes an arc-shaped plate arranged obliquely and bent towards the filter plate. The top of the arc-shaped plate is fixedly connected to the top of the depressed plate, and the spaced distance between the arc-shaped plate and the filter plate is more than 10 cm.


Preferably, the filtering device also includes a water return pipe. One end of the water return pipe is connected to a collecting pipe, and the other end is connected to the water inlet pipe. The water return pipe is provided with a water return valve.


Preferably, the filter plate in the filter unit corresponding to the upper layer deflector has a larger filter hole than the filter plate in the filter unit corresponding to the adjacent lower layer deflector, which is conducive to the effective interception and removal of impurities of different particle sizes and further improves filtration efficiency.


Preferably, the filter plate in the filter unit corresponding to the upper layer deflector has a smaller filter hole than the filter plate in the filter unit corresponding to the adjacent lower layer deflector.


The advantages of the invention are as follows.


(1) The filtering device has a simple structure. By spatially stacking multiple layers of filter plate units and setting the filter plates 52 into inclined curved filter plates 52, the problem of clogging that easily occurs in the filter plates can be alleviated. This saves space and improves filtration efficiency of the diatomite mixed solution. By installing the deflector 30 and the depressed plate 40, the water distribution can be made more uniform thus alleviating the accumulation of the diatomite mixture unevenly distributed on the filter plate 52 due to uneven water distribution, which can further avoid the clogging of the filter plate and improve the filtration efficiency of the device.


(2) The present invention facilitates the effective interception and removal of impurities with different particle sizes by combining materials of the filter plate 52 with different pore sizes in different filter plate units, thereby further improving the filtration efficiency. Taking the two-layer filter unit as an example, the filter plate 52 in the upper filter plate unit adopts a large filter hole structure, and the filter plate 52 in the lower filter plate unit adopts a small filter hole structure. In use, the water distribution valve 21 corresponding to the upper filter plate unit is first opened, and the water distribution valve 21 corresponding to the lower filter plate unit is closed. The diatomite mixture is filtered once by the upper filter plate unit to remove large particles of impurities. Then, the water distribution valve 21 corresponding to the lower filter plate unit is opened, and the water distribution valve 21 corresponding to the upper filter plate unit is closed. The primary filtered water is subjected to secondary filtration through the water return pipe 70. The water inlet pipe 10 and the lower filter plate 52 unit to remove small particles of impurities.


(3) The filter residue trapped after being filtered by the filtering device of the present invention can slide along the slag guide plate 54 through the hydraulic impact of the incoming water and then fall and the filter residue easily cleaned. In addition, the present invention can clean and remove slag from one of the filter units without affecting the work of other filter units.





BRIEF DESCRIPTION OF THE DRAWINGS


FIG. 1 is a structural diagram of the present invention;



FIG. 2 is a side view of the present invention;



FIG. 3 is a structural diagram of a filter unit in the present invention;



FIG. 4 is a structural diagram of a filter unit in the present invention;





Reference numerals are as follows:



10. water inlet pipe; 20. shunt pipe; 21. water distribution valve; 30. deflector; 31. shell; 311. water inlet; 312. overflow port; 313. diversion folding plate; 32. top plate; 40. depressed plate; 51. water guide groove; 511. water collecting port; 512. water collecting space; 52. filter plate; 53. upper shutter; 54. slag guide plate; 60. water collecting pipe; 70. water return pipe; 71. water return valve; 80. water outlet pipe.


DETAILED DESCRIPTION OF THE EMBODIMENTS

A specific embodiment of the present invention is described in detail with reference to FIGS. 1 to 4, but does not limit the claims of the present invention in any way.


As shown in FIGS. 1 to 4, a filtering device for removing impurities in a mixture of biological diatomite includes the water inlet pipe 10, the shunt pipe 20, the plurality of deflectors 30, the filter unit and the water collecting pipe 60.


The plurality of deflectors 30 are evenly distributed in multiple layers in the vertical direction. Each deflector 30 includes the shell 31 and the top plate 32, and the left and right sides of each deflector 30 are symmetrically provided with a filter unit.


The shell 31 is provided with the top plate 32, and the top plate 32 is hinged with the depressed plate 40 through a hinge. The bottom of the shell 31 is provided with the water inlet 311. The water inlet 311 is communicated with the shunt pipe 20. The water distribution valve 21 is provided on the shunt pipe 20, and the overflow ports 312 are provided on the upper left and right side walls of the shell 31. The plurality of diversion folding plates 313 are horizontally arranged under the overflow port 312, and the plurality of diversion folding plates 313 are staggered and distributed on the left and right side walls of the shell 31 in the vertical direction.


The filter unit includes the water guide groove 51, the filter plate 52 and the upper shutter 53. The water guide groove 51 is inclined and fixedly connected to the wall of the shell 31. The water guide groove 51 in the filter unit located on the left side of the shell 31 is fixedly connected to the left side wall of the shell 31, and the water guide groove 51 in the filter unit located on the right side of the shell 31 is fixedly connected to the right side wall of the shell 31. The water collecting space 512 with an open top is formed between the water guide groove 51 and the side wall of the shell 31. The water collecting port 511 is provided on the front groove wall of the water guide groove 51, and the water collecting port 511 communicates with the water collecting pipe 60. In order to increase the water collecting space 512 of the water guide groove 51, the bottom of the water guide groove 51 is set as an arc surface.


The filter plate 52 is located in the water collecting space 512. The filter plate 52 is inclined and fixedly connected to the side wall of the shell 31. The top of the filter plate 52 is flush with the bottom of the overflow port 312, and the bottom of the filter plate 52 is flush with the top of the right wall of the water guide groove 51. The slag guide plate 54 is smoothly connected to the bottom end of the filter plate 52. In order to increase the filtering area of the filter plate 52 and improve the filtering efficiency of the filtering device, the filter plate 52 is provided as an arc-shaped mesh plate curved toward the water collecting space 512.


The upper shutter 53 functions as a cover. The upper shutter 53 includes an arc-shaped plate that is inclined and bent toward the filter plate 52. The arc-shaped plate is located above the filter plate 52, and the spaced distance between it and the filter plate 52 is greater than 10 cm. The top of the curved plate is fixedly connected to the top of the water pressure plate 40.


The water inlet pipe 10 is connected to each branch pipe 20.


The water outlet pipe 80 is connected to the water collecting pipe 60, and the water outlet pipe 80 is provided with a water outlet valve.


In order to improve the filtering effect of the device on the impurities in the biological diatomite mixed solution, the filtering device is further provided with the water return pipe 70. The two ends of the water return pipe 70 connect with the water collecting pipe 60 and the water inlet pipe 10, respectively. The water return valve 71 is provided on the water return pipe 70. During operation of the device, the water outlet valve is closed. The water return valve 71 and the water distribution valve 21 are opened, so that the filtered water once filtered by the filter unit can pass through the water collecting pipe 60, the water return pipe 70 and the shunt pipe 20 in sequence. The filtered water then may enter the filter unit again for secondary filtration to improve the water quality of the effluent from the filtering device.


The filter plate in the filter unit corresponding to the upper layer deflector has a larger or smaller filter hole than the filter plate in the filter unit corresponding to the adjacent lower layer deflector to effectively intercept and remove impurities with different particle sizes in the biological diatomite mixture and further improve the filtration efficiency.


How it works:


The sewage (biological diatomite mixture) enters the deflector 30 through the water inlet pipe 10, the water distribution valve 21 and the shunt pipe 20 in sequence. Through the rectification and energy dissipation of the diversion folding plates 313 in the deflector 30. The sewage flows out uniformly from the overflow port 312 of the deflector 30. Under the function of secondary rectification and energy dissipation of the depressed plate 40, the sewage flows out uniformly from the lower side of the depressed plate 40 and is filtered through the filter plate 52 from top to bottom. The water filtered by the filter plate 52 enters the water guide groove 51, and flows into the water collecting pipe 60 through the water collecting port 511. The filter residue trapped after being filtered by the filter plate 52 slides along the residue guide plate 54 by the hydraulic impact of the incoming water and then falls.


The implementations mentioned above are only for the purpose of illustrating the present invention, and are not intended to limit the present invention. Those ordinary skilled in the prior art may make various changes and modifications, without departing from the essence and scope of the present invention. Therefore, all equivalent technical solutions should also belong to the scope of the present invention.

Claims
  • 1. A filtering device for removing impurities in a mixture of biological diatomite, comprising a water inlet pipe, a plurality of shunt pipes, a plurality of deflectors, a filter unit and a water collecting pipe, wherein the plurality of deflectors are evenly distributed in a plurality of layers in a vertical direction, each deflector of the plurality of deflectors comprises a shell and a top plate, and a left side and a right side of each deflector of the plurality of deflectors are symmetrically provided with the filter unit; a top of the shell is covered with the top plate, and the top plate is hinged with a depressed plate through a hinge, a bottom of the shell is provided with a water inlet, the water inlet pipe is in fluid communication with each of the plurality of shunt pipes, a water distribution valve is provided on the plurality of shunt pipes, and a plurality of overflow ports are provided on upper portions of a left side wall and a right side wall of the shell;a plurality of diversion folding plates are horizontally arranged under the plurality of overflow ports, and the plurality of diversion folding plates are staggered and distributed on the left side wall and the right side wall of the shell in the vertical direction; the filter unit comprises a water guide groove and a filter plate, the water guide groove and the filter plate are fixedly connected to a side wall of the shell, the water guide groove is arranged obliquely, a water collecting space with a top opening is formed between the water guide groove and the side wall of the shell, a water collecting port is arranged on a front groove wall of the water guide groove, and the water collecting port is connected to the water collecting pipe;the filter plate is obliquely arranged in the water collecting space, a top of the filter plate is flush with a bottom of the plurality of overflow ports, and a bottom of the filter plate is flush with a top of a right groove wall of the water guide groove; anda water outlet pipe is connected to the water collecting pipe, and the water outlet pipe is provided with a water outlet valve.
  • 2. The filtering device according to claim 1, wherein a bottom of the water guide groove is a curved surface.
  • 3. The filtering device according to claim 1, wherein the filter plate is an arc-shaped mesh plate and the arc-shaped mesh plate is curved toward the water collecting space.
  • 4. The filtering device according to claim 1, wherein the filter plate is a screen with a clearance of 0.5-5 mm grid or mesh no less than 50 mesh.
  • 5. The filtering device according to claim 1, wherein the bottom of the filter plate is connected to a slag guide plate.
  • 6. The filtering device according to claim 1, wherein the filter unit further comprising an upper shutter for covering, the upper shutter comprises an arc-shaped plate, the arc-shaped plate is arranged obliquely and bent towards the filter plate, a top of the arc-shaped plate is fixedly connected to a top of the depressed plate, and a spaced distance between the arc-shaped plate and the filter plate is more than 10 cm.
  • 7. The filtering device according to claim 1, further comprising a water return pipe, a first end of the water return pipe is connected to a collecting pipe, a second end of the water return pipe is connected to the water inlet pipe, and the water return pipe is provided with a water return valve.
  • 8. The filtering device according to claim 7, wherein the filter plate in the filter unit corresponding to an upper layer deflector has a larger filter hole than the filter plate in the filter unit corresponding to an adjacent lower layer deflector.
  • 9. The filtering device according to claim 7, wherein the filter plate in the filter unit corresponding to an upper layer deflector has a smaller filter hole than the filter plate in the filter unit corresponding to an adjacent lower layer deflector.
Priority Claims (1)
Number Date Country Kind
202010008273.6 Jan 2020 CN national
US Referenced Citations (224)
Number Name Date Kind
311485 Gridley et al. Feb 1885 A
566260 Wightman Aug 1896 A
571776 Long Nov 1896 A
678857 Betzold Jul 1901 A
690082 Snyder Dec 1901 A
786184 Benefield Mar 1905 A
955843 Bossert Apr 1910 A
968242 Inman Aug 1910 A
1104772 Black Jul 1914 A
1333127 Nall Mar 1920 A
1360834 Wallace Nov 1920 A
1424451 Crandall Aug 1922 A
1510742 Gutleben Oct 1924 A
1653473 Schulz Dec 1927 A
1725511 Flanagan Aug 1929 A
1803112 Helfenbein Apr 1931 A
1990214 Zapffe Feb 1935 A
2090997 French Aug 1937 A
2095504 Kesti Oct 1937 A
2133974 Cowles Oct 1938 A
2158169 Wright May 1939 A
2308572 Symons Jan 1943 A
2317430 Ayers Apr 1943 A
2419501 Pinto Apr 1947 A
2450006 Lesniak Sep 1948 A
2463814 Skinner Mar 1949 A
2494780 Schmidt Jan 1950 A
2748941 Basten Jun 1956 A
2814388 Dreissen Nov 1957 A
2872041 Dreissen Feb 1959 A
2883051 Maeder Apr 1959 A
2916142 Fontein Dec 1959 A
2942730 Fontein Jun 1960 A
2973865 Cibula Mar 1961 A
2984356 Bruninghaus May 1961 A
3007574 De Koning Nov 1961 A
3124530 Jakobs Mar 1964 A
3135690 Eder Jun 1964 A
3221877 De Koning Dec 1965 A
3259244 Kaljo Jul 1966 A
3261470 Daniels Jul 1966 A
3307698 Haffner Mar 1967 A
3344919 Leeman Oct 1967 A
3353674 Leeman Nov 1967 A
3363769 Wilmot Jan 1968 A
3420658 Berhenke Jan 1969 A
3446349 Benzon May 1969 A
3451555 Ginaven Jun 1969 A
3452876 Ginaven Jul 1969 A
3477571 Maag Nov 1969 A
3483974 Pearsall Dec 1969 A
3572505 Jongbloed Mar 1971 A
3640383 Wantling Feb 1972 A
3712476 Cohen-Alloro Jan 1973 A
3777893 Ginaven Dec 1973 A
3813298 Chwalek May 1974 A
3815740 Ginaven Jun 1974 A
3833123 Walker Sep 1974 A
3835999 Moore Sep 1974 A
3859713 Fiedler Jan 1975 A
3928207 Wace Dec 1975 A
3929642 Ennis Dec 1975 A
3929647 Kempa Dec 1975 A
3970549 Ennis Jul 1976 A
3982499 Frankl Sep 1976 A
3993567 Ginaven Nov 1976 A
4039456 Stoev Aug 1977 A
4042511 Ginaven Aug 1977 A
4046694 Ellis Sep 1977 A
4065382 Derrick, Jr. Dec 1977 A
4071193 Sternby Jan 1978 A
4097382 Cruea Jun 1978 A
4113626 Detcher Sep 1978 A
4120790 Tinker Oct 1978 A
4122001 Snyder Oct 1978 A
4128474 Ennis Dec 1978 A
4190678 Pleus Feb 1980 A
4193503 Connolly Mar 1980 A
4202777 Schall May 1980 A
4233159 Senda Nov 1980 A
4250024 Soares Feb 1981 A
4250038 Dryden Feb 1981 A
4268382 Hanke May 1981 A
4274952 Hanke Jun 1981 A
4297213 Airey Oct 1981 A
4300445 Hazen Nov 1981 A
4319993 Krause Mar 1982 A
4376044 Ditzenberger Mar 1983 A
4415462 Finch Nov 1983 A
4422937 Connolly Dec 1983 A
4437982 Wasson Mar 1984 A
4447325 Pauley May 1984 A
4505812 Lees Mar 1985 A
4512880 Connolly Apr 1985 A
4519902 Kinder May 1985 A
4584099 Burton Apr 1986 A
4592275 Frankl Jun 1986 A
4661253 Williams Apr 1987 A
4666602 Hartzell May 1987 A
4671877 Godbeer Jun 1987 A
4710296 Connolly Dec 1987 A
4826017 Du Bourg May 1989 A
4840728 Connolly Jun 1989 A
4857176 Derrick Aug 1989 A
4863597 Gilles Sep 1989 A
4902409 Clark Feb 1990 A
4944873 Williams Jul 1990 A
4961864 Bruke Oct 1990 A
4981587 Moorhead Jan 1991 A
4990249 Leuenberger Feb 1991 A
4997566 Davis Mar 1991 A
5013429 Krofta May 1991 A
5076921 Bailey Dec 1991 A
5098557 Hirschler Mar 1992 A
5108626 Lees Apr 1992 A
5156749 Williams Oct 1992 A
5197263 Midtling Mar 1993 A
5246579 Probstmeyer Sep 1993 A
5255790 Einoder Oct 1993 A
5268100 Hartzell Dec 1993 A
5279736 Moorhead Jan 1994 A
5330643 Webb Jul 1994 A
5354467 Moorhead Oct 1994 A
5413709 Webb May 1995 A
5425876 Rector Jun 1995 A
5429247 Lemay Jul 1995 A
5451315 Miller Sep 1995 A
5531889 Baron Jul 1996 A
5547569 Spencer Aug 1996 A
5575913 Sharkey Nov 1996 A
5624038 Curtis Apr 1997 A
5674386 Filion Oct 1997 A
5709051 Mazziotti Jan 1998 A
5746322 LaVeine May 1998 A
5749471 Andersson May 1998 A
5765696 Pryor Jun 1998 A
5779887 Rector Jul 1998 A
5819951 Sultanovich Oct 1998 A
5904843 Herbst May 1999 A
6024870 Thompson Feb 2000 A
6063296 Ackerman May 2000 A
6095338 Connolly Aug 2000 A
6325215 Anthony Dec 2001 B1
6354442 Obst Mar 2002 B1
6497816 Naddy Dec 2002 B2
6511595 Crompton Jan 2003 B2
6531057 Houle Mar 2003 B1
6540911 Bajema Apr 2003 B1
6619312 Doiron Sep 2003 B2
6672462 Sharkey Jan 2004 B2
6705049 Esmond Mar 2004 B2
6749068 Dias Jun 2004 B1
6773612 Dias Aug 2004 B2
6830155 Trench Dec 2004 B2
6863181 Dias Mar 2005 B2
6892891 Dias May 2005 B2
6926839 Sharkey Aug 2005 B2
6936164 Wade Aug 2005 B2
6953529 Weir Oct 2005 B2
6986849 Irvine Jan 2006 B2
7122119 Gribble Oct 2006 B2
7258785 Weir Aug 2007 B2
7300590 Weir Nov 2007 B2
7303672 Irvine Dec 2007 B2
D575853 Adamson Aug 2008 S
7455784 Irvine Nov 2008 B2
D589127 Cornwall Mar 2009 S
7550077 Graf Jun 2009 B2
7584577 Esmond Sep 2009 B2
7708494 McLaughlin May 2010 B2
7799231 Irvine Sep 2010 B2
7805890 Esmond Oct 2010 B2
7882959 Augst Feb 2011 B1
7919002 Hurtado Apr 2011 B1
8033058 Block Oct 2011 B2
8404110 Block Mar 2013 B2
8418856 Bailey Apr 2013 B2
8557127 Houle Oct 2013 B2
8562832 Houle Oct 2013 B2
8747666 Miller Jun 2014 B2
8757392 LaVeine Jun 2014 B2
8813968 Mandeville Aug 2014 B1
9233398 Dahl Jan 2016 B2
9260321 Garios Feb 2016 B2
9409208 Convery Aug 2016 B2
9427780 Houle Aug 2016 B2
9457381 Gordon Oct 2016 B2
9567719 Doyle Feb 2017 B2
9682334 Bioton Jun 2017 B2
9908147 Flansburg Mar 2018 B2
10125496 Lenney Nov 2018 B2
10695800 Lazzarini Jun 2020 B2
10791869 Al-Shaibani Oct 2020 B2
10953437 Herzog Mar 2021 B2
11066798 Paczek Jul 2021 B2
20010004973 Asakawa Jun 2001 A1
20010013492 Dias Aug 2001 A1
20020153334 Sharkey Oct 2002 A1
20020175120 Norell Nov 2002 A1
20020195377 Trench Dec 2002 A1
20030094424 Dias May 2003 A1
20030116511 Dias Jun 2003 A1
20030127375 Gribble Jul 2003 A1
20030167700 Esmond Sep 2003 A1
20040222167 Weir Nov 2004 A1
20040245152 Dias Dec 2004 A1
20050072738 Weir Apr 2005 A1
20050246967 Esmond Nov 2005 A1
20060150531 Cann Jul 2006 A1
20080086953 Graf Apr 2008 A1
20080101867 McLaughlin May 2008 A1
20090236273 Esmond Sep 2009 A1
20100038300 Allan Feb 2010 A1
20100270219 Block Oct 2010 A1
20110278217 Inoue Nov 2011 A1
20110303307 Block Dec 2011 A1
20110315623 Motakef Dec 2011 A1
20130105369 Houle May 2013 A1
20130105409 Houle May 2013 A1
20130105413 Houle May 2013 A1
20180055289 Al-Shaibani Mar 2018 A1
20190070636 Lazzarini Mar 2019 A1
20200392687 Paczek Dec 2020 A1
20210205741 Dai Jul 2021 A1
Related Publications (1)
Number Date Country
20210205741 A1 Jul 2021 US