The present invention relates to wastewater treatment systems and improvements thereto. More particularly, this invention relates to an apparatus for treatment of primary effluent from residential and commercial establishments to allow subsurface or surface disposal of wastewater therefrom.
Many areas in this country are experiencing an increase in population accompanied by a larger demand for housing and commercial establishments in rural areas and around major municipalities with no access to a public sewer system. Conventional onsite wastewater systems provide a viable option for managing the wastewater generated by development, however, not all soils are suitable for these systems. Conventional onsite wastewater systems also require a large land area, putting a premium cost on real estate in many locations. In order to maintain a non-hazardous environment, residential and commercial establishments must treat wastewater that they produce. Since public utility wastewater treatment systems and conventional onsite systems are not always available or are not desirable, alternative wastewater treatment methods are often necessary. Due to the premium price on real estate and the high density of residential and commercial building, it is desirable to reduce and minimize the space required for wastewater treatment systems to treat the wastewater to acceptable standards.
According to an illustrated embodiment of the present invention, a wastewater treatment apparatus comprising a recirculation chamber, a dosing chamber having no direct fluid connection to the recirculation chamber, and a filter layer containing a filter media and being located above the recirculation and dosing chambers. The recirculation chamber, the dosing chamber, and the filter layer are located in a single tank. The apparatus also comprises an influent pipe that directs wastewater entering the wastewater treatment apparatus into the recirculation chamber, and a recirculation pump located in the recirculation chamber. The recirculation pump pumps the wastewater from the recirculation chamber onto the filter layer. The apparatus further comprises a septic tank return pipe connected to the dosing chamber, a portion of the wastewater being discharged from the wastewater treatment apparatus through the septic tank return pipe back to a septic tank for additional treatment, and an effluent discharge pipe connected to the dosing chamber. Wastewater is discharged from the wastewater treatment apparatus through the effluent discharge pipe for final disposal.
In an illustrated embodiment, a wastewater treatment unit includes a tank having an interior region, and a divider located in the interior region of the tank to divide the interior region of the tank into two distinct chambers including a recirculation chamber and a dosing chamber having no direct fluid connection to said recirculation chamber. A first filter layer containing filter media is located above said recirculation chamber, and a second filter layer containing filter media is located above said dosing chamber. An influent pipe is provided which directs wastewater entering said wastewater treatment unit into said recirculation chamber. A recirculation pump is located in said recirculation chamber. The recirculation pump pumps the wastewater from the recirculation chamber onto said first and second filter layers. An effluent discharge pipe is connected to said dosing chamber. Wastewater is discharged from said wastewater treatment unit through said effluent discharge pipe for final disposal.
Additional features of the invention will become apparent to those skilled in the art upon consideration of the following detailed description of the best mode of carrying out the invention as presently perceived.
The detailed description particularly refers to the accompanying figures in which:
Referring now to the drawings, settled and screened wastewater from a septic tank or other primary treatment device enters the recirculation chamber 28 through influent pipe 48. The influent wastewater mixes with treated water falling from recirculation filter section 20 through underdrain 50 and is stored in the recirculation basin 36. The mixture of influent wastewater and treated effluent flows to recirculation pump 68. Recirculation pump 68 pumps the wastewater through distribution pipe 58 into the recirculation filter 54 which removes larger particles and prevents clogging of distribution piping and orifices, a typical filter being a model STF-100A2 pressure filter with a available from GAG Sim/Tech located in Boyne City, Mich. After passing through recirculation filter 54 the wastewater passes through a distribution pipe union 56 and enters the filter distribution pipe tee 57. The wastewater flow is split in filter distribution pipe tee 57 and is discharged into recirculation chamber distribution piping 61 and dosing chamber distribution piping 62, passing through recirculation distribution ball valve 59 and dosing distribution ball valve 60. Wastewater then flows through recirculation chamber distribution piping 61 and dosing chamber distribution piping 62 and is discharged from recirculation distribution pipe orifices 63 and dosing distribution pipe orifices 64. The recirculation distribution pipe orifices 63 and dosing distribution pipe orifices 64 discharge the wastewater upwards through recirculation chamber airspace 66 and dosing chamber airspace 67 and against the bottom of tank cover 92, which aerates the wastewater and distributes it across the recirculation filter section 20 and dosing filter section 21 and onto recirculation media 52 and dosing filter media 53.
A recirculation pump riser pipe 32 made of plastic or other lightweight material sets on recirculation filter underdrain 50 and prevents the recirculation filter media 52 from falling into the recirculation pump basin 38 and recirculation basin 36. A hole, slightly smaller than the diameter of recirculation pump riser pipe 32 is cut into recirculation filter underdrain 50 to allow recirculation pump 68 and distribution piping 58 to be lowered into place in recirculation basin 36. A filter distribution pipe union 56 on distribution piping 58 allows the recirculation pump 68, distribution piping 58 and recirculation filter 54 to be removed from recirculation basin 36 for servicing without entering the recirculation pump basin 38. Recirculation chamber distribution piping 61 can be periodically flushed out to prevent the buildup of solids in the piping by turning on recirculation pump 68, closing dosing distribution ball valve 60 and opening recirculation distribution piping flush valve 80 to flush recirculation chamber distribution piping 61 back into the recirculation pump basin 38. Dosing chamber distribution piping 62 can be periodically flushed out to prevent the buildup of solids in the piping by turning on recirculation pump 68, closing recirculation distribution ball valve 59 and opening dosing distribution piping flush valve 82 to flush dosing chamber distribution piping 62 back into the recirculation pump basin 38.
A recirculation basin level control 70, located in the recirculation chamber 28 measures the water level in the recirculation basin 36. A preferred recirculation basin level control is a pressure transducer. A typical pressure transducer is a submersible, stainless steel 4-20 mA output model available from Measurement Specialties, Inc. located in Hampton, Va. When the water level in the recirculation basin 36 reaches a programmed minimum level above the floor of recirculation chamber 28 as measured by recirculation basin level control 70, control panel 16 activates recirculation pump 68 to begin pumping to recirculation filter section 20 and dosing filter section 21 on a programmable time interval. The timed doses will repeat on a programmed schedule as long as the water level in the recirculation basin 36 remains above the programmed minimum level above the floor of recirculation chamber 28. If the water level in the recirculation basin 36 rises above a programmed maximum level above the floor of the recirculation chamber 28 as measured by recirculation basin level control 70, control panel 16 activates recirculation pump 68 to operate until a programmed drop in water level in recirculation basin 36 is achieved. If the water level in recirculation basin 36 does not drop after a programmed time or the level continues to rise, control panel 16 will signal a high recirculation basin alarm by activating an alarm light, audio alarm and a telephone dialer within control panel 16 to call and alert a service representative.
The wastewater discharged from recirculation distribution pipe orifices 63 and dosing distribution pipe orifices 64 is distributed over recirculation filter section 20 and dosing filter section 21 and flows through the recirculation filter media 52 and dosing filter media 53 by gravity. As the wastewater flows through the filter media it is treated by a combination of physical, chemical and aerobic biological processes. A preferred media is textile chips. Illustratively, the recirculation filter media 52 and dosing filter media 53 is a non-woven textile fabric composed of polyethylene filaments such as Type 4-17PE textile chips available from Texel, Inc. located in Quebec, Canada.
The treated effluent from recirculation filter section 20 flows through recirculation filter underdrain 50 consisting of fiberglass grating or materials of a similar design and falls back into the recirculation basin 36. The treated effluent from dosing filter section 21 flows through dosing filter underdrain 51 and falls into dosing basin 40. The placement of chamber dividing wall 22 within tank 12 determines the size of the recirculation chamber 28 and the dosing chamber 30. The areas of recirculation filter section 20 compared to the area of the dosing filter section 21 determines the recirculation ratio of the wastewater treatment apparatus 10. For example, if the recirculation filter area 20 is 40 square feet in size and the dosing filter section 21 is 10 square feet in size, the recirculation ratio would be equal to 40 square feet divided by 10 square feet and would create a recirculation ratio of 4:1. Typical recirculation ratios range from 3:1 to 5:1. The number of recirculation distribution pipe orifices 63 and dosing distribution pipe orifices 64 shall be in the same proportion as the recirculation ratio. For example, if there are 40 recirculation distribution pipe orifices in the 40 square feet recirculation filter section of the above example, there would need to be 10 dosing distribution pipe orifices in the 10 square feet dosing filter section of the same example.
A dosing basin level control 74 located in the dosing chamber 30 measures the water level in the dosing basin 40. A preferred dosing basin level control is a pressure transducer. A typical pressure transducer is a submersible, stainless steel 4-20 mA output model available from Measurement Specialties, Inc. located in Hampton, Va. When the water level in the dosing basin 40 reaches a programmed minimum level above the floor of the dosing chamber 30, the dosing basin level control 74 signals the control panel 16 to begin pumping to the effluent discharge pipe 76 on a programmable timed basis until a programmed level of water has been removed from the dosing basin 40. The doses will repeat on a programmed schedule as long as the water level in the dosing basin 40 remains above the programmed minimum level above the floor of the dosing chamber 30. If the water level in the dosing basin 40 rises above a programmed maximum level above the floor of the dosing chamber 30, the dosing basin level control 74 signals the control panel 16 to start dosing pump 72 and pump until a programmed drop in level is achieved. If the level in the dosing basin 40 does not drop after a programmed time or the level continues to rise, the control panel 16 will signal a high dosing basin alarm by activating an alarm light, audio alarm and a telephone dialer within control panel 16 to call and alert a service representative.
The treated filter effluent falling into the dosing basin 40 from dosing filter section 21 flows through the dosing chamber 30 to dosing pump 72. The dosing pump 72 pumps the treated effluent through the effluent discharge pipe 76 into a treated effluent filter 78, a typical filter being a model STF-100A2 pressure filter with a 100 micron sock available from GAG Sim/Tech located in Boyne City, Mich. The treated effluent passing through the treated effluent filter 78 is directed to discharge system 90 via effluent discharge pipe 76.
A dosing pump riser pipe 34 made of plastic or other lightweight material sets on dosing filter underdrain 51 and prevents the dosing filter media 53 from falling into the dosing pump basin 42 and dosing basin 40. A hole, slightly smaller than the diameter of dosing pump riser pipe 34 is cut into dosing filter underdrain 51 to allow dosing pump 72 and effluent discharge pipe 76 to be lowered into place in dosing basin 40. An effluent discharge pipe union 88 on effluent discharge pipe 76 allows the dosing pump 72, effluent discharge pipe 76 and treated effluent filter 78 to be removed from dosing basin 40 for servicing without entering the dosing pump basin 42.
An optional tablet chlorinator 84 consisting of a polyvinyl chloride pipe with slots located in the bottom of the pipe below the low water elevation may be located in the dosing chamber 30. The tablet chlorinator is filled with chlorine disinfectant tablets and capped at the top. The water flowing through the dosing basin 40 when dosing pump 72 is operating moves through the slotted pipe containing the chlorine tablets and slowly dissolves the tablets while imparting a chlorine residual in the treated effluent. The chlorine residual acts to disinfect the treated effluent by killing the pathogenic organisms in the effluent. The hardness and percentage of chlorine in the tablets can be regulated to produce the proper chlorine residual in the treated effluent to provide the necessary disinfection level. Alternately, other forms of treated effluent disinfection can be used such as ultraviolet light disinfection or ozonation.
Recirculation pump section riser 94 located over recirculation pump section 18 provides access to the recirculation pump 68 for maintenance. The recirculation pump section riser 94 is covered with recirculation pump section riser lid 98. Recirculation pump section riser lid includes recirculation pump section vent 104 to provide air to the recirculation pump section 18 while recirculation pump 68 is operating. Recirculation filter section riser 96 located over recirculation filter section 20 provides access to recirculation filter media 52, recirculation chamber distribution piping 61, recirculation filter underdrain 50 and recirculation basin 36. The recirculation filter section riser 96 is covered by recirculation filter section riser lid 100. Recirculation filter section riser lid 100 includes recirculation filter section vent 102 to provide free transfer of oxygen to recirculation chamber air space 66 and recirculation filter media 52.
Dosing pump section riser 106 located over dosing pump section 19 provides access to the dosing pump 72 for maintenance. The dosing pump section riser 106 is covered with dosing pump section riser lid 110. Dosing pump section riser lid 110 includes dosing pump section vent 116 to provide air to the dosing pump section 19 while dosing pump 72 is operating. Dosing filter section riser 108 located over dosing filter section 21 provides access to dosing filter media 53, dosing chamber distribution piping 62, dosing filter underdrain 51 and dosing basin 40. The dosing filter section riser 108 is covered by dosing filter section riser lid 112. Dosing filter section riser lid 112 includes dosing filter section vent 114 to provide free transfer of oxygen to dosing chamber air space 67 and dosing filter media 53.
Although the invention has been described in detail with reference to certain preferred embodiments, variations and modifications exist within the scope and spirit of the present invention as described and defined in the following claims.
This is a continuation-in-part of U.S. application Ser. No. 10/348,497, filed Jul. 31, 2003, now U.S. Pat. No. 6,974,536, which is a continuation-in-part of U.S. application Ser. No. 10/019,857, filed Nov. 9, 2001, now U.S. Pat. No. 6,616,832, which claims the benefit of PCT International Application No. PCT/US00/12615, filed May 9, 2000, and which is a continuation-in-part of U.S. application Ser. No. 09/309,047, filed May 10, 1999, now U.S. Pat. No. 6,132,599, all of which are expressly incorporated by reference herein. U.S. application Ser. No. 10/348,497 claims the benefit of U.S. Provisional Application No. 60/349,262 which is also incorporated by reference herein.
Number | Date | Country | |
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60349262 | Jan 2002 | US |
Number | Date | Country | |
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Parent | 10348497 | Jan 2003 | US |
Child | 11301467 | Dec 2005 | US |
Parent | 10019857 | Nov 2001 | US |
Child | 10348497 | Jan 2003 | US |
Parent | 09309047 | May 1999 | US |
Child | 10019857 | Nov 2001 | US |