SLURRY REMOVAL PROCESS IN THE WATER PURIFICATION TREATMENT AND FILTRATION EQUIPMENT FOR CARRYING OUT THE PROCESS

Abstract: The invention is relating to a slurry removal process in the water purification treatment and apparatus and filter elements for carrying out the process. The process of the invention effects the filtration of the sludge in the same containers used for packing the sludge, said containers acting also as filter elements, and the subsequent drying of the sludge in said containers and outside the said filtration treatment. The invention provides a first sludge filtration stage in throw-away containers made of filter material, and a second sludge drying stage wherein drying of the sludge collected in said containers is effected outside the filtration unit so as to obtain through exhaustion of the material being treated without affecting operating times of the filtration unit. The process according to the invention is carried out by conveying the sludge into a series of bags made of filter material, until said bags are filled with sludge: the filtered water can be either recycled into the system or sent to discharge, whereas the filter bags are closed and stacked in the open air; natural evaporation of the liquid phase ensures the obtaining of a dried, hard product averaging not more than 30-40% - and even attaining as low as 20% - liquid contents is recovered solid products.

Description: SLURRY REMOVAL PROCESS IN THE WATER PURIFICATION TREATMENT AND APPARATUS AND FILTER ELEMENTS FOR CARRING OUT THE PRO CESS. This patent for an industrial invention is relating to a slurry removal process in the water purification treatment and apparatus and filter elements for carring out the process. During said purification treatment, sewage from both industrial and municipal effluences is subjected to a succession of process that are designed to remove noxious com ponents from said sewage before it is conveyed to the drai nage systems or to the natural water system. These purification processes generally involve chemical treatment of sewage with appropriate, coagulants promo ting sludge-flock formation, precipitation of said flocks in sedimentation tanks in which sewage sludge and the purified water to be discharged into drainage system are separated, and subsequent filtration of the sludge precipitated in the sedimentation tanks in order to remove as much water as pos sible from it, whereupon the liquid phase is readmitted to the water system, whereas the dried residue is discharged outdoors, or it is buried or treated for elimination. This invention is more specifically related to said filtration treatment of the sludge (also referred to as tur bid waters, slimy-or muddy.solution) settled down to the bot tom of sedimentation tanks. In this stage of the water purification treatment, the solid residue so separated should contain as minimum liquid as possible in order to reduce both the volumes and the costs required for removing such material. The conventional and most commonly used types of sludge filtration units are the filter presses, the rotary filters and the bag filters. The filter. presses consist of a succession of filter plates aligned on frames and through which the sludge is compelled to pass. These filtration units have the drawback that sludge tends to stick to the surface of filter plates which thus require manual removal of adhering sludge therefrom; the so removed product has to be col lected in convenient areas indoor the works and then packed in suitable containers for transportation purpose. The yield from a filtration unit of this type usually does not exceed 40% dry product. and higher yields would involve excessive sludge removal costs. The rotary filters consist of a cylindrical rotary drum which is partly immersed in a tank containing sludge: during the immersion the liquid product is drawn into the interior of the drum(pur.posedly wrapped up in a filter cloth) whereas the sludge is deposited in layers on the external surface of the drum. In this type of filters the solid product is automatically scraped off the drum surface, but manual intervention is in any case required for collecting and packing the slud ge; The rotary filter has moreover the disadvantage that its satisfactory working, depends on a continuous with slud ge. The yield of this filtration unit is generally limited to values of the order of about 20% dry product in the remo ved sludge. The bag filters consist of a number of filter cloth tu bes conveniently hold at their upper open end and mechanically closed at their bottom end. The muddy solution enters the upper open mouth of the bag filters and passes through the cloth in order to deposit sludge on its internal surface. At regular time intervals the hanging bag filters are opened at their. bottoms and the material contained therein is discharged in order to permit the filters to be further supplied with the slimy solution to be treated. This type of filter too has the disadvantage that it requires manual ope rations for removing sludge from the filtration unit, for moving the solid product to the collecting areas and for char ging it into containers or the like. In this case, too, the yield do not exceed, in general, 20% dry product in the slud ge, compatibly with the operating costs of the bag filters. Thus ,ail;#he above.descri traditional filtration units. present common difficulti#es concerning: removing sludge from filter elements, moving sludge to the collecting areas and its transport. These filtration units moreover imply not flexible dimensions (i.e. not adaptable to each individual case), as well as expensive and difficult maintenance opera tions. In addition, as stated herein before, per cent yields obtained by using these equipments are very low and, compati bly with the usually no-value of the removed sludge, they are hard likely yo be increased. This particularly implies that great volumes of sludge high in water contents are to be handled indoor the works with disadvantages concerning the type of containers to be used and the cost for taking the material away. The object of this invention is to provide a filtration process for removing sludge from turbid waters, which process does not require removing sludge from the filters, moving the sludge to collecting areas and an eventual packing operation: all of the above moreover ensures a dried final a product with yields substantially up to 80% dry matter perfectly packed, with no influence upon operating costs of the purification treatment equipment. The capacity of the invention to attain such high yield levels as mentioned above permits, moreover, the filtration of not thoroughly settled out turbid waters, or the treatment of a solid dispersion in hard decantable water. In fact, the invention will ensure satisfactory yields in dry product even from a material very high in liquid contents. The above and-other advantages are achieved by the pro cess for the removal of sludge according to the invention, wherein the process provides for the filtration of sludge directly in the same bags provided for the packing of sludge, and for subsequent drying of sludge in said bags and outside the filtration unit. Achieving filtration operations by utilizing -as filter elements- the same containers in which the sludge is packed permits the suppression of all the operations connected with detaching or scraping away muddy material from filter elements, moving and collecting said material in the conditioning areas, and introducing final product into packing containers. Provinding for.drying stage subsequent to filtration the pro cess ensures attainment of high, dry product yields wise unobtenable by filtration only. All of the above,with no interference in filtration times (the drying stage is ef fected outside the filtration unit so that this latter can operate independently of said drying stage), without increa sing operating costs of the equipment and even reducing them indeed (drying is accomplished by natural action; the packing containers act as filter elements, with obvious savings quantity of employed material; the sludge to be removed with less per cent moisture contents does not require the use of expensive containers suitable for transport purpose), and with the advantage of suppressing all pf the dif ficulties connected with the movement of a material high in water contents. The removal of sludge higher in dry product contents moreover turns into markedly reduced treatment costs. The process according to the invention is carried out by conveying the muddy solution into a set of bags (made of a filter material) until the bags are filled with the sludge: the definitively filtered water is conveyed to the drainage system, whereas the bags are closed and stacked outdoors; natur# evaporation of the liquid phase permits to obtain a dry and hard product; percentage of liquid decreases to 20% referred to the separated solid product. The process of the invention, for removal of sludge may be carried out as follows: the bags hanging from the supporting frame of the filtration unit are supplied with the muddy solution in order to obtain the separation of the sludge (which is collected inside the bag) from the water, which passes through the filter material. This first filtra tion operation may be conducted by filling the bag with the muddy solution and then allowing filtration to continue the bag being hanging, for 24-48 hours; in this case a pasty sludge is obtained (allowing to be shovelled), 20-30% dry. Otherwise the bags can be filled a first time, whereupon supply is stopped and filtration is allowed to continue for a few hours (e.g. 2h), then the bags are filled again, the supply with the muddy solution is stopped again and the filtration is allowed to continue for a longer time (e.g., 5h); the same operations as above are repeated once more, and filtration is allowed to go on for a even longer time (e.g., 9h); at last, the bags are filled again, and filtration goes on for 24-36 hours more. It is preferable to carry out the process of the inven tion by feeding the filter bags with the slimy solution each bag remains filled up for a desired length of time (e.g., 10-15h). Then, feeding is stopped and filtration is allowed to continue, the bags being hanging. Thereafter, the bags are withdrawn from the spouts to which they were hanged during the filtration stage, and the bags are closed at their mouth by the said of self-tightening or self-twistening rib bon ties, or the like: the sludge now is in filtered and pa cked condition. The bags are stacked on standard pallets, and the charged pallets ate stacked in stores, even in the open air. In this way, the sludge in the bags is allowed to reach a further dehydration stage which for the most takes place by evaporation Thus, sludges with a up to 80% dry-value can be obtained by the process method of the invention. The pallets carrying the bags with the now dried mate rial therein, can be charged then on usual transport vehicles in order to be delivered to disposal areas. The description of an illustrative and not restrictive way of esecution referred to a filter unit for carrying out the process of the invention is given below with references to the enclosed drawings, in which: - Figure 1 is a front view of a filter unit according to the invention; - Figure 2 shows, in a top view, the lower part of the fil ter unit in figure 1; - Figure 3 shows a filter-bag during the filtration stage; the bag having been filled with the muddy solution and re moved from the filtration unit in fig.1; - Figure 4 shows the manner in which the filter-bags -such as the one in figure 3- may be palletized during the dry ing stage of sludge; - Figure 5 is a filter-bag that has been opened up to show contents of the bag afther the drying stage. The filter unit shown in figures 1 and 2 includes a conventional type of decanter 1 which is provided as its bot tom part with a valve 2 and with a revolving feeder or spout 4 that is operated from a geared motor 3. A filtration batte ry unit 9, circular in shape, is installed beneath said decanter 1 and comprises a framework 7 set up a basement 10, this basement including a tank 11 and a pipe 8 for collecting and discharging the filtered water, respectively. On the circular rim of said frame 7 are placed inlet spout 5 to which filter-bags 6 are hanged through their mouths. The inlet spouds 5 are advantageously provided at their top with small.hoppers 12 wich make easier the flowing of the slimy solution into the bags. On starting the supply of filter-bags 6, suitable auto matisms (not shown) carry the revolving spout 4 on the mouths of the bags to be filled. Thus, discharged water is collected into tank 11 to be either recycled into the system or conveyed to the discharge. The filter-bags 6 can be made of any appropriate filter cloth obtained from a material -such as, for example a polyproprylene cloth- which is resistent and inert to chemi cals and bacteria; these bags are closed at the bottom,and have open mouths. The number of bags per basic unit can vary depending on the requirements of the purification treatment concerned, and several units can be installed in series or in parallel, and can be automatically charged at predeter mined times. With the above described equipment it is possible to carry out the process of the invention according to any requirement. For instance, the bags..can be filled only once and then the filtration goes on at rest; or the bags can be fil led in successive stages; or the bags can be fed so that they are kept filled for a predetermined length of time. Once the bags are filled, the bags are detached from their spouts 5, they are charged on pallets -such as the pallet 13- and the loaded pallets are stacked (see figure 4). When the sludge in the bags has attained the desired drying level (see figure 5), the filter-bags are charged on transport vehicles for removal to a dump. With the process and the equipment according to the in vention, filtration-dehydration of sludge goes on also out side the filtration unit, while as concerns bag filters,for. exemple dehydration of sludge stops on emptying the tubes and, thus, at still very high moisture levels. The ability of the invention to achieve combined filtration and packing of the sludge brings to a very important advantage of this process, as compared with conventional systems where the cost for emptying the filters adds to the cost of the containers in which the sludge has to be collected; the high moisture contents of this latter, in fact, require the employ of expensive containers which in turn frequently requi re higher transportation costs due to the specially suited transport vehicles that have to be provided for. Moreover, the process of the invention does no longer require such frequent cleaning operations as are necessary with the conventional filters which, due to the nature of the material being treated, have to be submitted to careful and expensive maintenance work at frequent intervals. The following example, which is given by way of illustration and is by no means restrictive to the scope of the invention, describes a case where a sewage from an industrial effluent was treated for removing sludge therefrom. Indications as to the residual moisture contents are only given as a specimen, as drying rate is determinantly affected by a number of variable elemnts such as concentration and type of substances making up the sludge, co-existence of different pollutants, flockes size, climatic conditions under which operations are carried out, and the like. EXAMPLE A plant was equipped for removing sludge from a waste ef fluent coming from an industry operating in the field of varnishes, paints and enamels, the waste effluent averaging a COD charge from 1500 to 2000 Kg/day and consisting of a suspension of about 5% dry product, in weight. Medium quali tative composition of the concerned sewage was as follows: - coagulated suspended varnishes - precipitated pigments - calcium.isuiphate - - insoluble salts of heavy metals. The filtration equipment was a twin filtration unit provided with a total number of 32 throw-away filter bags made with a spunbonded polypropylene with continous fibers (a product sold by DUPONT under the trade name "Typar"), each bag having a volume of about 75 1. The slimy solution was pumped into the filter-bags for 10-15h, then filtration was allowed to go on at rest, for a 3-day period. After the 3-days period of filtration, the bags contai 'ned about 80 Kg of sludge with a percentage of 20-25% dry product, in weight. The filter-bag utilized in the process according to the invention was found to be able to filter-a quantity of slimy solution 5% in weight equal to 4-5 times the volume of the bag within 2-3 days. Subsequently, the bags were removed from the filtration unit, tied at their mouths with self-tightening ribbons and charged on two throw-away pallets, placed in position 2+1-by-5-layers totalling 32 filter-bags. The charged pallets were put above another one and set aside for the time necessary to reach a suitable quantity for one delivery. After about 30 days the sludge was dehy- drated so as to attain 45-60% dry product contents (even up to 80%-dry in summer months), in weight. Each filter-bag, in which there were initially collected about 80 Kg of sludge 22,5% dry product in##ight,-con- tained 30 to 40 Kg of sludge- 45-60% dry product in weight after parking. After about 4 weeks more, the percentage of dry product in weight raised to 60-70%, and the residue was a hard, well dried -looking material. Subsequently, the bags were charged on a transport vehicle and taken away for delivery to a controlled dump area.

Claims: WEAT WE CLAIM IS: 1. A process for removing sludge in a water purification treatment, wherein the process comprises effecting fil tration of the sludge in the same containers which are used packing containers for the sludge and which also act as the filter elements, and subsequent drying of the sludge in said containers and outside said filtration treatment. 2. The process according to claim 1, wherein the pro-cess comprises a first sludge filtration stage in throwaway containers made of a filter material, and a second sludge drying stage in which the sludge, collected in said containers, is dried outside the filtration unit so as to obtain through exhaustion of the material being treated without affecting operating times of the filtration unit. 3. The process according to claim 1 and 2, wherein said sludge filtration stage is effected by sullying the filter-container with the slimy solution until said container is filled up, and allowing filtration fo the sludge col lected in said container to go on at rest for a predetermined time said predetermined time depending on the characteristics of the sludge. 4. The process according to claim 1 and 2, wherein said sludge filtration stage is realized filling a first time the filter-container with the sludge, stopping the supply and allowing filtration to go on for a predetermined time; then filling a second time said container with the sludge, stopping the supply and allowing filtration to go on for a longer time; and, finally, filling once more said container, stopping the supply and allowing filtration of the sludge to go on at rest in said container for a further predetermi ned time. 5. The process according to claims 1 and 2, wherein said filtration stage is realized filling the filter-contai ner with the sludge and going on with the supply so that the container is permanently kept filled during a desired lenght of time. 6. A filtration equipment for carrying out the process according to the preceding claims, wherein said equipment consists of one or a plurality of filtration units (9) moun ted in series or in parallel, each filtration battery unit consisting of a frame (7) substantially circular in shape as viewed from the above, said frame (7) being provided with inlet spouts (5) and with filter-containers (6) tightly fitted at their mouths to said inlet spouts (5), the basement (10) of said frame (7) including a receiving tank (11) and the pipe (8) for collecting and discharging the filtered water, respectively. 7. The equipment according to claim 6, wherein a decan ter (1) is placed above the filtration unit (9), said decan ter (1) being provided at the discharge outlet with a revol ving spout (4) for feeding the filter-containers (6), said filter-containers (6) being positioned beneath and facing to the discharge section of the revolving spout (4). 8. A filter element, wherein the filter element consists of a container beeing a bag with closed bottom and open mouth made of a resistent, inert filter material. 9. The filter element according to claim 8, wherein said container is made of a filter material of spumbonded polypropylene with continous fibers.

Inventors: CAMERINI, GIANNI
Applicants: NATRO CELLULOSA INDUSTRIA IMBALLAGGI CARTA S.P.A.
Application year: 1982
Main classification: B01D23
IPC codes: B01D29, B01D35