fig1 describes the five step / stage process of the invention described in fig1 . sewage 40 is obtained from a primary sewage treatment system which is or includes a filtering step to remove large objects , grit and the like and a sedimentation tank step to remove suspended settleable solids . activated polymer solution from inline polymer mixer 41 is injected into sewage 40 to aid in flocculation . the sewage 40 then moves into inline mixing - and - flocculating unit 42 wherein the sewage is mixed and flocculated to enhance chemically induced liquid - solids separation . the treated sewage exiting from mixing - and - flocculating unit 42 is subjected to chemical ph adjustment 43 by the addition thereto by a base such as lime or caustic ( potassium hydroxide or sodium hydroxide ). the ph of the sewage is adjusted into the basic ph range or to a higher basic ph . the sewage is then poured onto sand bed 44 which contains a support grid therein . the larger insoluble solids and flocks in the sewage collect on the top of sand bed 44 and the water in the sewage passes / filters through sand bed 44 . once the solids and flocks located on top of sand bed 44 dry , a layer of dried sludge pieces is obtained on top of sand bed 44 . the dried sludge pieces are then removed in sludge retrieval step 45 to provide dried sludge 46 . with regard to the first step of the invention process , that is , polymer mixing and injecting device ( see fig1 ) is more fully shown in fig2 . the polymer mixing - feeding ( injecting ) ( 165 ) system is an integrated equipment package which automatically meters , activates , dilutes and feeds liquid polymer and water . ( see fig2 and 6 .) concentrated polymer and water are blended in a complete high energy chamber . the prepared solution via tube ( 166 ) exits the original chamber ( 167 ) through the top of the vessel ( 168 ). it then re - enters an outer retention chamber ( 169 ) and exits the chamber ( 169 ) via tube ( 170 ) at the bottom of the vessel to the polymer injectors . a round access plate ( 171 ) is fabricated in the bottom of the primary chamber ( 167 ) for repair and service . the chamber ( 167 ) can be constructed of polyvinyl chlorides , stainless steel or any other suitable material . polymer from a source not shown is transported in tube ( 172 ) by means of metering pump ( 173 ). unit ( 173 ) mixes water with the polymer . the polymer is injected into the chamber ( 167 ) through a tube ( 172 ) passed through the top of the chamber ( 167 ). the tube ( 172 ) is designed to be adjustable in length giving variations in depth or placing the polymer closer to the aspirator or mixing energy . at the end of the tube ( 172 ), a spring loaded check valve ( 174 ) allows polymer to spray into the mixing area in a thin filming process ( 182 ). energy for polymer activation is created by a 5 / 8 inch or any size stainless steel hollow shaft ( 175 ) which at the end of the shaft is a polyvinyl chloride or stainless steel 4 - way aspirator ( 176 ). with the aspirator turning at 3 , 450 rpm , a tremendous vacuum occurs drawing free air down the hollow shaft ( 175 ) into the chamber ( 167 ). this process causes high energy mixing . the stainless steel shaft ( 175 ) is driven by a hollow core motor ( 177 ). the motor ( 177 ) and shaft ( 175 ) are attached by a coupler ( 176 ). the 5 / 8 inch or any size shaft ( 177 ) with aspirator ( 176 ) is placed inside the chamber ( 176 ) and that chamber ( 176 ) is made water tight with exterior mechanical seals ( 178 ). inline check ( 179 ) and ball valves ( 180 ) are installed on the top or inlet side of the motor ( 177 ). these valves ( 180 ) can regulate the amount of air passed through the hollow shaft ( 175 ) to the mixing chamber ( 176 ). the one way directional flow check valve ( 179 ) is used to prevent liquid from exiting through the aspirator ( 176 ) and shaft ( 175 ) when the motor ( 177 ) is in the off position . the mixer has a brass solenoid valve for on / off control of dilution water supply ( not shown ), and a rotameter - type flow indicator ( 181 ) equipped with integral rate - adjusting valve . water is supplied to primary chamber ( 167 ) via tube ( 183 ). the flow indicator is machined acrylic and has valve stop and guided float . water flow rate is adjustable 0 to 500 usgph . water supply input and stock solution output fittings are 0 to 500 fnpt . the drive motor ( 177 ) of the unit is powered by a 2500 watt generator producing 12ov - 15 amps . the generator ( not shown ) is mounted to the trailer and becomes a permanent fixture of the transportable system . with regard to the second step of the invention process , that is , inline mixing and flocculating ( see fig1 ), the following mixer - flocculating system is constructed : onto the bed of a trailer ( 110 ), the mixer - flocculating system ( 101 ) is secured . ( see fig4 .) part of the mixer - flocculating system is a mixer - flocculator unit ( 80 ). sewage enters pipe ( 102 ) the mixing - flocculator unit ( 80 ) through an elbow ( 103 ). the elbow ( 103 ) is attached to a vertical inlet pipe segment ( 104 ) which is , in turn , attached to another elbow ( 103 ). this latter elbow ( 103 ) has a flange ( 82 ) which is attached to a flange on the end of a downflow segment ( 105 ). the downflow segment ( 105 ) continues into a horizontal bottomflow segment ( 106 ). a recycle segment ( 111 ) contacts the downflow segment ( 105 ). an electrical control - drive unit ( 88 ) turns a threadedly adjustable rod ( 88a ) extending through the wall of the device to contact the top of adjustable baffleplate ( 87 ). baffleplate ( 87 ) is pivotally attached ( 87a ) to the side of to the downflow segment ( 105 ) near the top where the downflow segment ( 105 ) and recycle segment ( 111 ) intersect . the adjustable , nonflexible baffleplate ( 87 ) is located at an angle ( which can be readily changed ) within the downflow segment ( 105 ). ( see fig5 .) the electrical control - drive unit ( 88 ) can , instead , be a manual control ( of the angle of the adjustable baffleplate ), such as , manually turning the rod ( 88a ). the other end of the recycle segment ( 111 ) and the other end of the bottomflow segment ( 106 ) are joined to openings in a upflow segment ( 107 ). at one end of the upflow segment ( 107 ) is a flange ( 82 ) which is attached to a flange ( 82a ) at one end of an elbow ( 103 ). the other end of this elbow ( 103 ) is attached to a vertical , exit pipe segment ( 108 ). attached to the other end of the vertical , exit pipe segment ( 108 ) is another elbow ( 103 ) through which the sewage exits ( 109 ). running into the elbow ( 103 ) which is attached both to the vertical inlet pipe segment ( 104 ) and the downflow segment ( 105 ) are polymer or flocculant injection lines ( 84 ). attached to the other end of these polymer or flocculant injection lines ( 84 ) are a manifold ( 85 ), a quick connect ( 86 ), a motor ( 115 ) and a control valve ( 114 ). ( see fig6 .) a dip tube ( 113 ) runs from the control valve ( 114 ) into a barrel ( 112 ) resting on the trailer ( 110 ). preferably the polymer mixing and injecting apparatus of fig1 is used to provide the activated polymer solution to barrel 112 . sewage enters an elbow ( 103 ) and runs through the vertical inlet pipe segment ( 104 ). it then passes through another elbow ( 103 ) into the downflow segment ( 105 ). as the sewage / flow passes into the downflow segment ( 105 ), it passes through a 45 degree angle . this area is called mixing zone 1 ( 83 ). as the sewage / flow runs through the downflow segment ( 105 ), it encounters an adjustable baffleplate ( 87 ), which is positioned at an angle . the adjustable baffleplate ( 87 ) restricts the vessel &# 39 ; s flow by about 50 to about 80 percent , thus increasing the original flow velocity by as much as 600 percent . then , the sewage / flow is fanned in one direction -- towards the bottomflow segment ( 106 ). a fixed baffle ( 90 ), which restricts typically 40 percent of the vessel &# 39 ; s size , is positioned in the downflow segment and serves to oppositely direct and fan the passing sewage / flow . the area between the adjustable baffleplate and the fixed baffle is called mixing zone 2 ( 89 ). then , the sewage / flow is directed into a 45 degree round angle into the bottomflow segment ( 106 ). positioned within the bottomflow segment are at least two ( preferably , a number of ) fixed , horizontal baffles ( 92 ), the positioning of which cause the sewage / flow to pass under and over and under these fixed , horizontal baffles ( 92 ) in a serpentine flow pattern , thereby reducing the flow velocity . this area is called mixing zone 3 ( 93 ). the sewage / flow , then , enters the upflow segment ( 107 ) in a 45 degree round angle which causes the sewage / flow to move in a spiraling pattern . positioned in the upflow segment ( 107 ) is ( at least one ) fixed vertical baffle ( 96 ). mixing zone 5 is in the exit end of upflow pipe 107 where it bends to the horizontal . before the sewage / flow exits the mixer - flocculator unit ( 80 ), before it enters an elbow ( 103 ) and the vertical exit pipe segment ( 108 ), it passes a horizontal pipe / recycle segment ( 111 ) which causes a portion of the sewage / flow to divert through this line , because of the pressure drop caused by the adjustable inlet baffle ( 87 ) placed at an angle . the bypass velocity may be increased , if the size of the pipe is increased and with baffle adjustments . also before the sewage / flow exits the mixer - flocculator unit ( 80 ), before it enters an elbow ( 103 ) and the vertical exit pipe segment ( 108 ), but after it passes the horizontal pipe / recycle segment ( 111 ), it passes through a 45 degree angle . this area is called mixing zone 4 ( 99 ). recycle segment ( 111 ) has a smaller diameter than the rest of the pipes of the unit . a drainage plug ( 91 ) is present in the downflow segment ( 105 ), close to where the sewage / flow enters the bottomflow segment ( 106 ). a flush plug ( 95 ) is present in the upflow segment ( 107 ) close to where it joins together with the bottomflow segment ( 106 ). model rf6 of the mixing and flocculating unit 80 os basically shown in fig5 . note the two non - flexible baffles 92 located in the bottom of bottomflow segment 106 . the results of tests using model rf6 in dewatering test are given below in table 1 and 2 . table 1______________________________________mixing zones ( velocity versus feet per second ) g . p . m . zone 1 zone 2 zone 3 zone 4 zone 5______________________________________a ) 100 1 . 28 5 . 04 2 . 89 8 . 68 1 . 28b ) 150 1 . 92 7 . 56 3 . 83 13 . 10 1 . 92c ) 200 2 . 57 10 . 10 4 . 44 17 . 4 2 . 57______________________________________ table 2__________________________________________________________________________ baffle plate emulsion polymer position sludge polymer solution (% of filtrate dried sludgevelocity con . conc . conc . vessel floc size conc . (% and ( g . p . m .) (% t . s .) ( neat ) (%) dia ) ( sml ) (% t . s .) time ) __________________________________________________________________________a ) 100 2 % 55 % . 25 . 70 l 0 6 hrs .- 14 % 24 hrs .- 24 % 48 hrs .- 30 % 72 hrs .- 47 % 168 hrs .- 60 % b ) 150 2 % 55 % . 25 . 65 l 0 samec ) 200 2 % 55 % . 25 . 60 m 0 same__________________________________________________________________________ model rf8 is similar to model rf6 except it has a larger flow capacity and only has one nonflexible baffle 92 in the bottom of flow segment 106 ( located between the two baffles 92 in the top thereof ). the results of tests using model rf8 in dewatering tests are given below in tables 3 and 4 . table 3______________________________________mixing zones ( velocity versus feet per second ) g . p . m . zone 1 zone 2 zone 3 zone 4 zone 5______________________________________a ) 200 1 . 28 5 . 04 2 . 89 8 . 68 1 . 28b ) 300 1 . 92 7 . 56 3 . 83 13 . 10 1 . 92c ) 400 2 . 57 10 . 10 4 . 44 17 . 4 2 . 57d ) 500 3 . 31 12 . 60 5 . 55 21 . 7 3 . 21e ) 600 3 . 85 15 . 10 6 . 66 28 . 0 3 . 85f ) 700 4 . 49 17 . 60 7 . 77 30 . 4 4 . 49______________________________________ table 4__________________________________________________________________________ baffle plate emulsion polymer position sludge polymer solution (% of filtrate dried sludgevelocity con . conc . conc . vessel floc size conc . (% and ( g . p . m .) (% t . s .) ( neat ) (%) dia ) ( sml ) (% t . s .) time ) __________________________________________________________________________a ) 200 2 % 55 % . 25 . 70 l 0 6 hrs .- 12 % 24 hrs .- 22 % 48 hrs .- 35 % 72 hrs .- 45 % 168 hrs .- 65 % b ) 300 2 % 55 % 25 . 65 l 0 samec ) 400 2 % 55 % . 25 . 60 m 0 samed ) 500 2 % 55 % . 30 . 55 s 0 samee ) 600 2 % 55 % . 50 . 50 s 0 samef ) 700 2 % 55 % . 55 . 50 s 0 same__________________________________________________________________________ the sewage apparatus of u . s . pat . no . 5 , 248 , 416 ( howard ) is shown in fig1 . in the apparatus of howard , incoming liquid containing solids and recirculated liquid containing solids and flock fills the entire apparatus , including pipe 229 . the velocity going into the system is the same as that exiting the system . the path of the flow of material is down conduit 217 , through bottom conduit 220 , up conduit 224 , and then split so as to be partly recycled through the top pie ( 229 ) and partly passed on out conduit 224 , without any meaningful restrictions . item 220 is a moveable flutter or ledge and items 229a are fabricated rubber tumblers which bend with the flow and , thus , offer little or no restrictions in the flow paths . moveable 220 is located in down flow conduit 217 at the lower intersection point of recycle conduit 229 and down flow conduit 217 . through testing of the howard system , applicant has found that the howard system is not very effective in achieving its stated purpose and in solving its stated prior art problem . in contrast , the improvements of the instant invention include a mixer - flocculator unit having an adjustable baffleplate placed at an angle to the direction of flow of the incoming sewage ( containing , for example , 1 / 2 to 8 percent of solids ). the baffle plate restricts the flow area in downflow pipe segment 106 just before the intersection with recycle pipe segment 111 by about 50 to about 80 percent . this cross - sectional area adjustment process can increase the original flow velocity by as much as 600 percent or more . the pattern of flow of the combination of the incoming material and the recycle material , then , is moved in one direction . thereafter , flowing liquid is oppositely directed and fanned by a fixed , nonflexible baffle which restricts 40 percent or so of the internal size ( cross sectional area ) of the pipe . then , the liquid flow is directed into a 45 degree round angle which causes the liquid flow to turn and pass under and over and under fixed , nonflexible baffles in a serpentine flow pattern , thereby further reducing the velocity of flow in the pipe . thereafter , the liquid flow enters a 45 degree round angle which causes the flow to move upward in a spiraling pattern . the liquid flow , then , comes in contact with a fixed , nonflexible baffle . such baffle is located across from the entrance to a side or recycle pipe . as the upward liquid flow reaches such baffle and side horizontal recycle pipe , a portion of it to divert through this line by the action of such baffle and by the pressure drop caused by the adjustable inlet baffle plate in the down flow pipe segment 106 . the internal diameter of recycle pipe 111 is less than the internal diameter of down flow pipe 105 or upward flow pipe 107 . the bypass velocity in the recycle pipe can be increased by decreasing the size of the pipe and / or by adjusting the baffle . this recycle system allows the continued size growth of the floc . preferably the mixer - flocculator unit will have multiple injector ports at the influent end of the mixer , through which the activated polymer solution can be injected into the liquid - sludge slurry flow stream . the activated polymer and sludge will then be quickly but gently mixed by baffling energy dispersing action . the mixing action promotes large floc growth . a portion of the flocculated sludge , then , is re - circulated into the influent stream by a pressure drop zone to advance and increase the efficiency of the mixing - flocculating process . the device can be fabricated utilizing corrosion free polyvinyl chloride components , stainless steel , concrete , fiberglass , wood or any other suitable metal or other material . the interior baffles can be fabricated from polyvinyl chloride , stainless steel , concrete , fiberglass , wood or any other suitable metal or other material . with regard to the third step of the inventive process , that is , a chemical induced ph adjustment of the sewage exiting the mixer - flocculating system ( 101 ), the following is included : as the liquid / solids content exits the inline mixer - flocculator unit ( 80 ), an electronic or gear driven diaphragm pump ( not shown ) pumps liquid caustic or lime into the discharge line for example , 102 , 108 , 109 , etc .) of the flocculator - mixer unit ( 80 ). the ph of the sludge is increased to 12 by the chemical additive ( base ). the ph of the sludge will remain at 12 for 72 hours , and , during this period of time , the temperature will reach 52 ° c . and will remain at that temperature for at least 12 hours . at the end of the 72 hour period during which the ph of the sludge is above 12 , the sludge can be air dried to achieve a percent solids of greater than 50 percent . the liquid caustic or lime pump is present on the transportable dewatering trailer ( 110 ) with the mixer - flocculating system ( 101 ) and the polymer feed system and , thus , is easily transported . with regard to the fourth step of the invention process ( see fig1 ), enclosure 49 contains sand bed 44 . onto a layer of non - porous material ( 50 ), e . g ., concrete , a layer of porous material ( 53 ) is positioned . porous material ( 53 ) is used as a filter media and usually stone , crushed rock , ceramic shapes , slag and plastics of 1 to 6 inches , practically 2 to 4 inches , in size are used . stones or pebbles are preferred . at least one -- usually more than one -- projection of porous material ( 54 ) extends from the porous layer ( 53 ) into the layer of non - porous material ( 50 ). embedded in each projection channels ( 48 ) in porous material ( 54 ) is at least one non - porous pipe ( 55 ) having at least one hole ( 56 ) into which liquid can drain . a layer of sand ( 57 ) is positioned above the layer of porous material ( 53 ). the sand - cell media sections ( 65 ) are positioned above this layer of sand ( 57 ). sand is located in passageways 59 in sand cell grid ( 65 ). above each sand - cell media section ( 65 ) is placed a layer of sand ( 61 ). this layer of sand ( 61 ) is usually , though not necessarily , at least six inches in depth . walls ( 51 ) surround on all four sides of an area having one or more sand - cell media sections ( 65 )-- on wall 51 is shorter to allow a front loader or the like into the enclosure . each surrounding , dividing wall ( 51 ) extends upward from one or more footing supports ( 52 ) which are positioned , at least partially , in the layer of non - porous material ( 50 ). the top of each dividing wall ( 51 ) extends above the layer of sand ( 61 ) overlaying the sand - cell media section ( s ). on the top of each dividing wall ( 51 ) which runs between two enclosure areas having sand - cell media sections ( 65 ) is portable nozzle ( 62 ) which is used to pour sewage into the enclosures . each sand - cell media section ( 65 ) is made up of one or more sand - cells ( 58 ) having the same shape and size . typically , the sand - cell media section is made up of honeycomb - shaped sand - cells ( 58 ) which are joined together in a honeycomb formation ( i . e ., each sand - cell which is not in an outer layer , where it intersects ( 59 ) another sand - cell , it intersects three other sand - cells ). a channel ( 59 ) runs through the interior of each sand - cell . sewage is poured through the channel ( 62 ) into one or more enclosures 49 for sand beds 44 . the liquid permeates the outer sand layer , flows through the sand in the channels ( 59 ) in the grid 65 in the centers of the sand - cells , permeates the layer of sand beneath the sand - cell media , and permeates the pebble layer beneath that layer , leaving the collected sludge solids to dry from the sun and air . with regard to the fifth of the invention process ( see fig1 ), a sludge retriever ( 125 ) is used to separate the dried sludge layer ( 134 ) from the sand ( 61 ) in the sand bed ( 44 ). ( see fig1 .) an upper pivoted arm ( 130 ) is attached to a front - end loader , as is a lower pivoted arm ( 129 ). the other end of each of these pivoted arms is attached to a two cubic yard bucket / hopper ( 133 ). the lower side ( 137 ) of the bucket / hopper ( 133 ) slides along the sandbed slightly above or on the layer of dried sludge ( 134 ) being retrieved . the lower , front end ( 138 ) of this bucket / hopper ( 133 ) is upwardly slanted relative to the rest of the lower end . at the lower back end of the bucket / hopper is attached a rotary drum ( 135 ) including a shaft ( 126 ) around which a rotary ( 128 ), from which multiple raw of three inch tines / teeth ( 127 ) project , turns . as the rotary drum ( 135 ) turns ( clockwise ), pieces of dried sludge ( 134 ) and minimal amounts of sand ( 61 ) are tossed into the bucket / hopper ( 133 ). an arm ( 132 ) is attached to a ball pivot ( 131 ) which has a short arm ( 139 ) welded onto the end of ball joint ( 131 ). ball joint ( 131 ) is moved up or down in vertical slot ( 140 ) in the side of retriever ( 125 ) and moved and bolted into one of the three short horizontal slots ( 141 ), whereby shaft ( 126 ) is moved up or down to the desired position . this arrangement ( not shown ) is repeated on the other side of the retriever ( 125 ). in this manner , the height position of shaft ( 126 ) can be adjusted and accordingly the distance that vanes ( 127 ) extend below lower side ( 137 ) of retriever ( 125 ). as typically shown in fig1 , vane ( 127 ) extension levels of 1 inch , 2 inches and 3 inches are indicated by the marks &# 34 ; 1 &# 34 ;, &# 34 ; 2 &# 34 ; and &# 34 ; 3 &# 34 ;, respectively . the one inch level is usually used to chop up the dried sludge . the 2 inch level is shown in operation in fig1 . the three inch level is used , when the rotation direction of rotary ( 128 ) is reversed , to aerate the sand after the dried sludge has been removed . air flow grill or filter ( 136 ) is located in the top surface of bucket ( 133 ) near its front . with regard to the optional ( sixth ) step of the invention , that is , dewatering the sewage using an inline vertically - oriented , pneumatic dewatering tube ( 164 ) between steps ( a ) and ( b ) or ( b ) and ( c ) or ( c ) and ( d ), or before step ( a ), see fig1 . a cylindrical - shaped screen filter ( 150 ) reinforcing ribs ( 151 ), usually composed of stainless steel . rim rings ( 159 ) connect the circular - shaped screen filter ( 150 ) with a rim block ( 163 ). running through the rim ( 163 ) are water exit passageways ( 158 ). the flanged ends of cylindrical shell ( 153 ) are bolted ( 161 ) together with rim block ( 163 ). in this shell ( 153 ) are peripheral air chambers ( 154 ) which traverse the entire circumference of shell ( 153 ). one end of the water exit passageways ( 158 ) opens into the area in between the shell ( 153 ) and filter ( 151 ). positioned in this area are staggered , pressurized air jets ( 152 ) communicating with air chambers ( 154 ). manifolds ( 155 ) are positioned outside of shell ( 153 ) and communicate with every other circular air chamber ( 154 ), and hence to every other bank of pressurized air jets ( 152 ). use of the pneumatic dewatering device or tube ( 164 ) involves conducting ( 160 ) the sewage into the central tube - shaped filter where solids in the sewage are caught on the filter ( 150 ) and part of the water in the sewage passes through the filter ( 150 ). air under pressure is blown from staggered , high pressure air jets ( 152 ) against the outer surface of the filter ( 150 ) to dislodge the solids collected on the inner surface of the filter ( 150 ). the blowing air jets ( 152 ) are alternated in on - off sequences in order to continuously provide regions of the filter for the water to come through unimpeded by blowing pressurized air . in an alternate form of the invention ( see fig1 , as opposed to that which is portrayed in fig1 ), there is not a liquid exit passageway ( 158 ) running through each rim ( 163 ) through which liquid sewage is dispelled ( 157 ). rather , there is a channel ( 162 ) for sewage to flow through the rim ( 163 ) from one section to another and then out the bottom . in connection with the figures , the following list of the names of the parts of the instant invention are noted : ______________________________________numbers parts , etc . ______________________________________40 sewage ; 41 inline polymer mixer ; 42 inline mixing and flocculating unit ; 43 chemical ph adjustment ; 44 sand bed ; 45 sludge retrieval ; 46 sludge ; 48 channels ; 49 sand bed enclosures ; 50 non - porous layer ; 51 dividing wall ; 52 support upon which dividing wall is positioned ; 53 porous layer positioned directly above non - porous layer ( 50 ); 54 projection of porous layer ( 54 ); 55 non - porous pipe ; 56 hole in non - porous pipe ( 56 ); 57 layer of sand underlaying sand - cell media section ; 58 single sand - cell ; 59 channel running through interior of single sand - cell ; 60 point of intersection of 4 individual sand - cells ; 61 layer of sand overlaying sand - cell media section ; 62 channel into which sludge is poured63 loader or other loading equipment ; 64 wheel of loader or other loading equipment ; 65 sand - cell media section ; 80 mixer - flocculator unit ; 81 input conduit ( influent end of mixer ); 82 flanges ; 82a flange ; 83 mixing zone 1 ; 84 polymer or flocculant injection lines ; 85 manifold ; 86 quick connect ; 87 adjustable baffleplate placed at an angle ; 87a pivot attachment ; 88 electrical unit ; 88a threadedly adjustable rod ; 89 mixing zone 2 ; 90 fixed , vertical baffle ; 91 drainage plug ; 92 fixed , horizontal baffles ; 93 mixing zone 3 ; 94 walls ; 95 flush plug ; 96 fixed , vertical baffle ; 97 mixing zone 5 ; 98 recirculation baffles ; 99 mixing zone 4 ; 100 output conduit ; 101 mixer - flocculating system ; 102 liquid in ; 103 elbows ; 104 vertical inlet pipe segment ; 105 downflow segment ; 106 bottomflow segment ; 107 upflow segment ; 108 vertical exit pipe segment ; 109 liquid out ; 110 transportable dewatering trailer ; 111 recycle segment ; 112 barrel ; 113 dip tube ; 114 motor ; 115 control valve ; 125 sludge retriever ; 126 shaft ; 127 multiple 3 inch tines / teeth ; 128 rotary ; 129 lower pivoted arm attaching sludge retriever to front - end loader ; 130 upper pivoted arm attaching sludge retriever to front - end loader ; 131 ball pivot ; 132 arm ; 133 two cubic yard bucket / hopper ; 134 dried sludge ; 135 rotary drum ; 136 air flow grill or filter ; 137 lower side ; 138 front end ; 139 arm ; 140 vertical , slot ; 141 show horizontal slots ; 150 screen filter ; 151 rib ; 152 high pressure air jet ; 153 wall ; 154 circular air chamber ; 155 manifold ; 156 pressurized air in ; 157 liquid sewage out ; 158 liquid exit ring ; 159 rim ring ; 160 passageway for sewage ; 161 bolt ; 162 channel for sewage ; 163 rim ; 164 inline pneumatic dewatering tube ; 165 polymer mixing - feeding system ; 166 tube ; 167 inner chamber ; 168 vessel ; 169 retention chamber ; 170 exit tube ; 171 access plate ; 172 tube ; 173 water - polymer mixing unit ; 174 check valve ; 175 hollow shaft ; 176 aspirator ; 177 motor ; 178 seal ; 179 check valve ; 180 ball valve ; 181 flow indicator ; 182 filming process ; and183 tube . ______________________________________ in connection with the figures , the following list of the names of the parts of a prior art invention [ u . s . pat . no . 5 , 248 , 416 ( howard )] are noted : ______________________________________212 upper right hand conduit / system input ; 214 multiple polymer ejectors ; 217 conduit ; 220 moveable flutter or ledge ; 222 conduit ; 222a conduit ; 224 conduit ; 226 output conduit / system output ; 229 recirculating conduit ; 229a pivotal flaps on recirculating conduit ; and230 support bracing . ______________________________________