Liquid purification or separation – Processes – Treating by enzyme
Reexamination Certificate
2003-01-22
2004-05-11
Hruskoci, Peter A. (Department: 1724)
Liquid purification or separation
Processes
Treating by enzyme
C210S721000, C210S727000, C210S734000, C210S737000
Reexamination Certificate
active
06733674
ABSTRACT:
TECHNICAL FIELD
This invention concerns the use of cellulolytic enzymes in combination with one or more oxidants and one or more flocculants to aid in dewatering municipal and industrial sludges.
BACKGROUND OF THE INVENTION
The dewatering of municipal and industrial sludges containing suspended organic solids is typically accomplished by mixing the sludge with one or more chemical reagents in order to induce a state of coagulation or flocculation of the solids which are then separated from the water using mechanical devices such as plate and frame filter presses, belt-filter presses, centrifuges, and the like.
For example, in a typical municipal sewage plant, waste water remaining after coarse solids are settled out of the incoming sewage influent is conveyed into a biological clarifying stage, where the dissolved and suspended organic material is decomposed by microorganisms in the presence or absence of air. These processes are referred to as aerobic digestion and anaerobic digestion, respectively.
The organic matter obtained as a result of this decomposition is largely bound in the form of a mass of microorganisms. This mass is precipitated as an activated sludge. The water may be released into waterways or allowed to seep away in sewage irrigation fields, but the activated sludge must be dewatered prior to disposal.
The objective of dewatering processes is to maximize the efficiency of water removal, as decreasing the amount of water retained in the dewatered solids leads decreased transport and disposal costs. Therefore, there is an ongoing need for improved dewatering technologies.
Dewatering of biologically-clarified sludges using a hydrolytic enzyme preparation containing cellulases followed by a high molecular weight cationic flocculant is disclosed in European Patent No. 291 665.
SUMMARY OF THE INVENTION
In its principal aspect, this invention is directed to a method of dewatering sludge comprising
i) adding an effective amount of one or more cellulolytic enzymes, one or more oxidants and one or more flocculants to the sludge to form a mixture of water and coagulated and flocculated solids and
ii) separating the coagulated and flocculated solids from the water.
DETAILED DESCRIPTION OF THE INVENTION
The cellulolytic enzyme preparation used in the practice of this invention are commercially available enzymes obtained from microorganism cultures. The preparations may contain a single cellulolytic enzyme or mixture of cellulolytic enzymes. Additional hydrolytic enzymes including proteases, glycoproteinases, lipases, alpha-amylases, beta-glucanases, hemicellulases, laminarinases, and the like may also be present as impurities in the enzyme preparation.
The cellulolytic enzymes useful in the practice of this invention include one or more cellulases present in the enzyme system that hydrolyzes cellulose to glucose, including endo-1,4-beta-glucanase, exo-1,4-beta-glucanase and 1,4-beta-glucosidase.
In a preferred aspect of this invention, the cellulolytic enzyme is a mixture of endo-1,4-beta-glucanase, exo-1,4-beta-glucanase and 1,4-beta-glucosidase.
In another preferred aspect, the cellulolytic enzyme is endo-1,4-beta-glucanase.
In addition to the cellulolytic enzyme(s), one or more oxidants capable of promoting oxidation of aromatic and non-aromatic moieties present in the sludge is added to enhance dewatering and potentially reduce the required cationic charge of the flocculant utilized.
Oxidants useful in this invention include both chemical oxidants and enzymatic oxidants.
Representative chemical oxidants include potassium permanganate, hydrogen peroxide, sodium peroxide, ammonium persulfate, manganese dioxide, and the like. A preferred chemical oxidant is potassium permanganate.
Suitable oxidative enzymes include peroxidase, laccase, tyrosinase, and the like.
Peroxidases useful in the practice of this invention are selected from the group of enzymes that use organic hydroperoxides or hydrogen peroxide as the oxidant to oxidize phenols to dimers via oxidative coupling. Representative peroxidases include peroxidases extracted from vegetables such soy bean and horseradish, as well as peroxidases from fruits such as apples and bananas and bacterial and fungal peroxidases. Peroxidases are also manufactured from bacteria and fungi.
Laccases, also known as para phenol oxidases, catalyse the oxidation of aromatic compounds where phenolic hydroxy groups are present only at the para position.
The catalytic center (active site) consists of three types of copper with different functions: type 1 (blue copper) catalyses the electron transfer, type 2 activates molecular oxygen and type 3, a copper dimer, is responsible for the oxygen uptake. Oxidation of the substrates by laccase leads to polymerization of the products through oxidative coupling. Products of oxidative coupling reactions result from C—O and C—C coupling of phenolic reactants and also from N—N and C—N coupling of aromatic amines. Laccases are mostly produced by white rot fungi. They may also be produced by plants and bacteria.
Tyrosinases catalyse the oxidation of aromatic compounds where phenolic hydroxy groups are located at the ortho and meta positions. They are commonly known as ortho-phenol oxidases. Similar to laccase, tyrosinases also have copper on its active site.
The effective doses of cellulolytic enzyme(s) and oxidant depend on the properties of the sludge being treated and can be empirically determined by one of skill in the art. In general, the dose of cellulolytic enzyme(s) is from about 20 to about 60 grams, preferably from about 40 to about 60 grams per dry ton of solids.
The effective dose of chemical oxidants is typically about 0.5 to about 5 pounds per ton, preferably about one pound per ton of oven dried sludge.
The effective dose of enzymatic oxidants is typically about 17 to about 50 grams, preferably about 25 to about 50 grams per dry ton solids.
The cellulolytic enzyme and oxidative enzymes are generally available as solutions in water, which can be further diluted. In the process of this invention, aqueous solutions having an enzyme concentration of from about 0.01 to about 100 grams of enzyme protein per liter are typically used.
Hydrogen peroxide is required to activate peroxidase. Dosages of hydrogen peroxide are typically from about 300 to about 1,000 milliliters preferably from about 500 to about 1,000 milliliters (based on a 30% aqueous hydrogen peroxide solution) per dry ton of solids.
For laccase, a mediator such as 2,2′-azino-bis(3-ethylbenzothiazine-6-sulfonic acid), commonly known as ABTS, is preferably used to obtain a satisfactory reaction rate.
In a typical application, the sludge to be dewatered is warmed to about 30° C. to about 60° C., preferably about 30° C. to about 40° C. with mixing. An aqueous solution of the celluloytic enzymes, prepared as described above is then added. After a period of about 10 minutes to several days, an aqueous solution of the chemical oxidant or an aqueous solution of the oxidative enzymes and any required activators and mediators are added together to the mixed sludge. Mixing and heating are then continued for about 2 hours to several days, after which time the sludge is cooled to ambient temperature and the flocculants and any coagulants are added. The sludge is mechanically dewatered, for example by devices such as plate and frame filter presses, belt-filter presses, centrifuges, and the like.
Suitable flocculants for use in this invention generally have molecular weights in excess of 1,000,000 and often 20,000,000. The polymeric flocculant is typically prepared by vinyl addition polymerization of one or more cationic monomers, by copolymerization of one or more cationic monomers with one or more nonionic monomers, or by polymerization of the cationic monomers with one or more anionic monomers and optionally one or more nonionic monomers to produce an amphoteric polymer.
While the polymer may be formed as a cationic polymer, it is also possible to react certain non-ionic vinyl addition polymers to produce cationically charged polymers. Po
Ramesh Manian
Sarkar Jawed
Shah Jitendra
Breininger Thomas M.
Hruskoci Peter A.
Martin Michael B.
Ondeo Nalco Company
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