A COMPOSITION FOR PURIFICATION TREATMENT OF WASTE WATER, AND A METHOD FOR PREPARATION THEREOF.
Field of the Invention This invention relates to a composition to be used for purification treatment of waste industrial waters, sewer waters, surface and underground waters, as well as to a specific method for preparing this composition, substantial characteristic of such method being the order according to which the individual components of the composition are added and the admixing procedure thereof.
Description of the invention
This invention relates to the purification treatment of contaminated water resulting from various sources, such as the industrial source waters, the municipal source waters (sewer waters) and broadly all waters containing contaminant materials, of organic or inorganic type.
The problem of water contamination is a long lasting problem, which is particularly severe in ail circumstances where a water supply is needed and, in this respect, a complete range of processes and products are available in the prior art for their purification treatment. The purification treatment methods for waste waters differentiate from one another according both to the type and the amount of contaminant materials contained in the waters to be treated and to the final contents thereof in the waters resulting from the treatment, such contents obviously depending on the desired final use of the waters resulting from the treatment.
Without deeply analysing the details of the individual stages of the prior art methods and of the functions of the various treatment products, it is believed sufficient to mention in this respect the substantial principles of the coagulation and flocculation processes that are determinative of the water treatment times.
In most practical cases, the waters to be treated contain contaminant materials in the form of colloids dispersed in solution or suspension, due to the electric charges existing on their surfaces as well
suspension, due to the electric charges existing on their surfaces as well as to their chemical-physical type interactions with the waters themselves (solvatation) which make the formation of larger particles and consequently their coagulation with resulting precipitation and sedimentation impossible.
During coagulation, any very small particles and colloidal materials, upon eliminating their surface charges hindering their agglomeration, cluster themselves together to form clots and flocks that are sufficiently big for them to precipitate and to be collected upon filters. A flock develops an active adsorbent effect on colloids that results into coloration of the water, on bacteria, on any other undesirable substances that are consequently removed. The coagulation can be natural, can be caused by softly stirring the waters rich in organic substances and in iron, or it can be obtained by chemical means, usually by adding suitable amounts of a coagulant agent selected among iron, aluminium or calcium salts, in order to form flocks of insoluble hydroxides or basic salts. The amount of the coagulant agent depends on the chemical and physical characteristics of the waters to be treated, on the equipment and on the apparatuses or tanks to be used. If it is desired to improve the characteristics of the coagulation flocks, it is convenient to add polymeric or copolymeric components having different chemical and physical characteristics, that can be of neutral type (polyacrylamide), of anionic type (polyacrylates) or of cationic type (alkyl ammonium polymeric salts). The function of these polymers or copolymers is substantially to form bridges between the coagulation flocks, thereby causing an increase in their size with consequent increase in their sedimentation speed.
Even if processes and products for purification treatment of waste waters are well known in the art, many drawbacks still exist in their application. The main drawbacks and disadvantages are due to the long times needed for coagulation and flocculation, up to sixteen hours, to not satisfactory clarification of the waters, to permanence of disagreeable
odours in the waters after their treatment as well as to the presence of residual muds that tend to form solid deposits.
In view of all above, it is the object of this invention to provide a particular material composition adapted to eliminate all above mentioned drawbacks and disadvantages and to enable a rapid and effective purification treatment of industrial waste waters, of the municipal sewer waters as well as of any surface or underground waters.
It has been found that, particularly when the composition of this invention is used together with suitable apparatuses, which are no part of the present invention, it is possible to perform a continuous purification treatment of said waste waters, by feeding the waters to be purified to the apparatus inlet and by collecting the treated waters having the desired purity characteristics from the apparatus outlet.
The composition includes the following components and it is prepared by admixing the components in the following order:
1) Calcium hydroxide (Ca(OH)2) in powdered form in the range of about 60 to 90% by weight,
2) active vegetable carbon in the range of about 10 to 20% by weight, 3) aluminium sulphate hydrate (AI2(SO4)3 x 18H2O) in the range of about 7 to 11 % by weight,
4) homopolymers of acrylamide or copolymers of acrylamide and salified acrylic acid in the range of about 0.1 to 1 % by weight.
According to a specific preferred embodiment of this invention, the composition includes:
75 % Ca(OH)2 in powdered form, 15 % active vegetable carbon in powered form, 9.5 % AI2(SO )3 x 18 H2O as crystals,
0.5 % homopolymers of acrylamide or copolymers of acrylamide and salified acrylic acid.
Copolymers of acrylamide and salified acrylic acid suitable for use in the composition according to this invention correspond to the following broad formula
m
and they are commercially available under the designations Ecoclar 8001 , 8002 and 8003 from Ausimont S.p.A., at Milan, Italy.
As previously mentioned, even if the waste waters to be purified can be of various sources (waters for domestic use, including hygienic and sanitary waters and therefore waters mixed with solid and liquid residuals, rain water as well as waters produced as waste residuals of industrial processes) and even if such waters can have various chemical and microbiological compositions, they can possibly be preliminary subjected to conventional treatment processes (preparatory treatment, sifting, sand removal, oil removal), in respect of coarse solids, and to a primary treatment (primary sedimentation), in respect of finer solids, and thereafter they all will be subjected to the same treatment with use of the composition of this invention.
The purification process is carried out as follows. The composition according to this invention is added to and dispersed in the water to be treated in amount of 1% or more, according to the contamination level, and the resulting dispersion is stirred at room temperature. An immediate clarification of the water is obtained in view of the combined effects of flocculation and coagulation developed by the aluminium sulphate hydrate and by the organic polymers included therein, which form flocks of mixed composition (hydroxides, salts, insoluble bases adsorbed on the polymer macromoiecules). The pH value of the waters is generally around 9 due to the presence of calcium hydroxide. During the homogenisation process, the particles of active vegetable carbon develop an adsorption activity, thereby eliminating all organic substances, the hydrogen sulphide (H2S), the mercaptans and any malodorous effluent components. In few seconds, two layers are formed: a layer of purified water, which is suitably recovered and reused, and a layer of shovelable
muds, having very low toxicity characteristics, that can be further treated in order modify their physical characteristics, while their final intended use, for which an enhancement step can also be provided (use in agricultural field, recovery of valuable substances, composting, anaerobic digestion, pyrolysis, disposal into sea water or in a controlled dump or burning or burial), will depend of course on the source of the waters subjected to the purification treatment.
From the preparation method view point, as above mentioned, it has been found that the order according to which the individual components are added and the mixing level extended to optimum homogeneity after addition of each individual component are essential for the obtainment of a product capable to furnish the above quoted performances and adapted to long lasting storage while its performance characteristics remain unaltered. It has been found that, if, after addition of each individual component, the composition is not mixed to homogeneity, it is not possible to obtain at the end of the preparation process a globally homogeneous composition capable to furnish optimum performances.
Furthermore, it has surprisingly found that if bentonite is used, in stead of the calcium hydroxide or of a portion of it, by maintaining the above quoted percentages of the sum of both components in the final resulting formulation, the final composition is capable of the same performances in a purification treatment of waters.
This is effectively surprising in view of the known different chemical and physical characteristics of both components. By summarising the advantages that can be obtained by exploitation of the teachings of this invention, it can be said that
- a higher flocculation and clarification speed is obtained, together with
- an extended coagulation and adsorption range, under neutralisation of all bad odours (about 85%) with a single composition, - less amounts of mud residuals having very low toxicity and
- low operation costs.
This invention has been described by way of illustration and not by way of limitation according to its preferred embodiments, but it should
expressly be understood that those skilled in the art can make variations and/or changes, without so departing from the scope thereof, as defined by the enclosed claims.