CN1303355A - Method for treatment of aqueous streams comprising biosolids - Google Patents

Method for treatment of aqueous streams comprising biosolids Download PDF

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Publication number
CN1303355A
CN1303355A CN99806750.4A CN99806750A CN1303355A CN 1303355 A CN1303355 A CN 1303355A CN 99806750 A CN99806750 A CN 99806750A CN 1303355 A CN1303355 A CN 1303355A
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acid
organic polymer
biosolids
current
anionic
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CN100360437C (en
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R·H·莫菲特
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EIDP Inc
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EI Du Pont de Nemours and Co
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56—Macromolecular compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Peptides Or Proteins (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

A process is provided which can be used to clarify substantially aqueous streams and optionally separate biosolids, especially proteins, from food processing operations which comprises contacting an aqueous stream comprising biosolids with an anionic inorganic colloid and an organic polymer, to flocculate the biosolids.

Description

The treatment process of aqueous streams comprising biosolids
Relevant U. S. application
The application is the further part of the U.S. Patent Application Serial 09/086,048 submitted on May 28th, 1998.
Background of invention
Invention field
The present invention relates to a kind of clarification and process from animal, the method for the main moisture working fluid stream of bird processing and so on food-processing operation particularly relates in particular to from wherein separating bio solid, particularly protein.
Description of Related Art
In food-processing operating period, the large number of biological solid, as protein, carbohydrate, fat and oil accumulation in current, for example from the animal slaughtering field of food mfg and other food-processing operation, as the waste water or the washing water of proteins extraction during the soyabean processing etc.This current from source mill must be through clarification, promptly separates and removes suspended solids reclaiming value product, or just can enter in city or the public water system after the clarification.After separation and drying, this biosolids can be used as in animal-feed, crops fertilizer, medicine and the individual health care product etc.In a specific examples, the protein that reclaims from soybean can be used as junior food.
This class biosolids is by the granulometric composition of belt surface electric charge.In general, this particle is with the anion form surface charge when alkalescence or pH neutral.The repulsive force that surface charge produces between the particle keeps separately particle.For the individual particles of colloid size, as protein, gravity deficiency so that they from aqeous suspension, precipitate.Simple separation method as filtering, can't be separated this protein solid, maybe can pass through filter screen because they can stop up filter screen.Therefore, make the discharging low and/or waste water stream of proteinic Separation and Recovery rate not meet environmental requirement.
The technology of removing deproteinize, carbohydrate, fat and oil and other biological pollutant from the food-processing current is known.A kind of method commonly used is by using metal-salt, and particularly the flocculating effect of molysite and/or aluminium salt and anionic polymer is separated protein, fat and oil from current.Because normal protein, carbohydrate, the fat and oily that reclaims that adopts in the animal-feed is so exist hygienic issues when coming the separating bio solid with metal-salt.Contained high-content metal salt in the biosolids that problem is to reclaim can accumulate in edible their animal tissues, and this class tissue continue after eaten by the mankind.Thereby Animal nutrition scholar also worries metal-salt and can combine the reduction nutritive value with the phosphorus in the feed.Food-processing industry attempts to find another kind of method, replaces with metal-salt isolated protein, carbohydrate, fat and oil from current.
Do not need just can clarify the current from food processing plant with metal-salt though disclose already, and therefrom isolate some kinds of methods of biosolids, its shortcoming is that each all can only just be enough to clarify this current with expensive material and long reaction times.The invention provides a kind of economy and effective means is clarified the food-processing current, and separate subsequently can commercial exploitation with recovery protein.
Summary of the invention
The invention provides a kind of method, for example be used for clarifying the current that comprise biosolids, this method comprises allows a kind of current that comprise biosolids contact with the following material of significant quantity:
(a) anionic inorganic colloid; With
(b) organic polymer, wherein, described organic polymer is selected from cationic polymers, amphiphilic polymers and their mixture, and its number-average molecular weight is greater than 1,000, and 000; Thereby form the flocculating biosolids.
If wish, can allow this current contact, so that the pH value of these current drops to below 7 with a kind of acid.In a specific embodiments of the present invention, allow current contact anionic inorganic colloid and sour simultaneously to reduce the pH value.Organic polymer contacts with these current and makes the biosolids flocculating then, so just the biosolids of flocculating can be separated from current.
Biosolids generally is suspended in the current because of surface charge effect.Surface charge depends on the pH value.The present invention also provides a kind of method, comprises allowing the current of the biosolids that contains the belt surface anionic sites in number contact with the following material of significant quantity:
(a) first organic polymer, wherein said first organic polymer is a cationic polymers, purpose is to reduce the number in the surface negative charge site on the biosolids, thereby makes biosolids be with some positively charged ion sites at least;
(b) anionic inorganic colloid; And
(c) second organic polymer, wherein said second organic polymer are selected from cationic polymers and amphiphilic polymers and their mixture; Thereby form the flocculating biosolids.In addition, when anionic inorganic colloid was the silicon dioxide base colloid, described second organic polymer can be selected from following one group: cationic polymers, anionic polymer and amphiphilic polymers, and their mixture.
Detailed Description Of The Invention
Many source mill produce the current that comprise protein, carbohydrate, fat and oily and so on biosolids, this current must be treated with the biosolids of telling potential value and/or and then from factory, emit.This current usually are that food processing plant produces, and its solids content is about 0.01～5 weight %.The invention provides a kind of method of clarifying these class current, make the solid flocculating in this method, and can therefrom isolate biosolids, the latter can be used to do animal feed etc. subsequently again.
As defined herein, flocculating is meant the biosolids of isolating suspension from the current that comprise biosolids, and wherein original biosolids that suspends becomes aggregate and separately is on the face of current or the bottom.The flocculating effect produces the flocculating material, if desired, can it be separated from current with physical method.Among the present invention, wish that the size of agglutinating matter is big as far as possible, make it to help it is separated from current.The material current
In the method for the present invention, the current that handle can comprise the source mill of the current of biosolids, for example food processing plant from any generation.For example, animal slaughtering and animal source mill and other food processing plant may produce and comprise protein, fat and oily current.Animal slaughtering field and source mill comprise the factory of butchering or processing ox, pig, bird and seafood.Other food processing plant comprises vegetables, grain and milk preparation source mill, for example, and the factory of soybean processing, rice, barley, cheese and serum; The water mill factory of starch and grain; And distillery.Existing biosolids in the current from these technologies outside isolating protein, fat and the oil, also may comprise sugar, starch and other carbohydrate.For example, in soyabean processing, protein is extracted feed water flow, therefrom reclaims again subsequently.The present invention comes from the current that animal is processed for processing, especially handles from the current of bird processing particularly useful.
Though the present invention is applicable to the traditional food process operation that produces the biosolids aqeous suspension, should be understood that the present invention is applicable to that also processing is from food (animal and vegetables) processing but the biosolids aqeous suspension that may have the non-food product end-use.For example, through separating and reclaiming, protein can be used in some makeup and other skincare product prescription; Starch has many kinds of non-food product purposes, comprises being used for papermaking.Further, the present invention is applicable to generally and handles any current that comprise biosolids that they may come from the non-food product process operation.And though as above disclosed, biosolids generally is suspended in the main moisture working fluid stream, also has the biosolids of suitable concentration can be dissolved in the current, and this depends on the character of current or biosolids, as pH value, salinity or other parameter.Anionic inorganic colloid
Be applicable to that the anionic inorganic colloid in the inventive method can comprise silicon dioxide base and non-silicon dioxide base anionic inorganic colloid and their mixture.The silicon dioxide base anionic inorganic colloid includes, but is not limited to colloid silica, aluminium modification colloid silica, polysilicate microgels, poly-silico-aluminate microgel, poly-silicic acid and poly-silicic acid microgel, and their mixture.Non-silicon dioxide base anionic inorganic colloid comprises clay, particularly colloid wilkinite.Other non-silicon dioxide base anionic inorganic colloid comprises colloid tin sulphate and titanyl sulfate.
Being used for anionic inorganic colloid of the present invention, can be to contain 2～60 weight %SiO that have an appointment 2, preferred about 4～30 weight %SiO 2Colloidal state silicon sol form.This colloid contains the particle that brings to few one deck silico-aluminate upper layer, perhaps also can be the silicon sol of aluminium modification.Colloidal silica particles in the colloidal sol, its specific surface area is generally 50～1000m 2/ g, more preferably from about 200～1000 m 2/ g, very preferably specific surface area is about 300～700 m 2/ g.Silicon sol can be used alkali stabilization, SiO 2: M 2The mol ratio of O is 10: 1～300: 1, and (M was Na, K, Li and NH in preferred 15: 1～100: 1 4).The granularity of colloidal solid is less than 60nm, and mean particle size is less than 20nm, and most preferably mean particle size is about 1nm～10nm.
The difference of microgel and colloid silica is: the specific surface area of micro-gel particles is generally 1000 m 2/ g or bigger, and microgel is connected to each other by the minor diameter silica dioxide granule of 1～2 nm, and chaining and three-dimensional network form.Polysilicate microgels also is called active silica, its SiO 2: Na 2The mol ratio of O is 4: 1～about 25: 1, and shows New York John Wiley﹠amp at Ralph K.Iler; Sons press is existing discussion in 174-176 page or leaf and the 225-234 page or leaf in " TheChemistry of Silica " (" silicon-dioxide chemistry ") of publishing in 1979.Poly-silicic acid is meant that generally the pH value is to form and partially polymerized and comprise the silica dioxide granule that diameter is generally less than 4nm at 1～4 o'clock, and these particles can aggregate into the silicic acid of chain and three-dimensional network subsequently again.Poly-silicic acid can be according to United States Patent (USP) 5,127, disclosed method preparation in 994 and 5,626,721, and these patents are incorporated herein for reference.Poly-silico-aluminate is in the particle or on the particle surface or the both has added the polysilicate or the poly-silicic acid microgel of aluminium.Polysilicate microgels, poly-silico-aluminate microgel and poly-silicic acid can prepare and stabilization under acid ph value.Have found that the result generally appears at the microgel size when big preferably; In general, the microgel greater than 10nm provides best performance.The microgel size can improve with any known method, the ageing of the microgel of knowing as those skilled in that art, changes change pH values, changes concentration or other method.
Be applicable to that polysilicate microgels of the present invention and poly-silicoaluminate microgel generally are by with a kind of alkali-metal silicate, at United States Patent (USP) 4,954,220 and 4,927, the condition described in 498 activates and forms, and these patents are incorporated herein for reference.But also can use other method.For example, poly-silico-aluminate can be as United States Patent (USP) 5,482, and 693 is described, and by coming acidifying silicate to form with comprising the mineral acid that is dissolved with aluminium salt, this patent is incorporated herein for reference.The alumina/silica microgel can be as United States Patent (USP) 2,234, and 285 is described, and by coming acidifying silicate to form with excessive alum, this patent is incorporated herein for reference.
Except traditional silicon sol and silicon-dioxide microgel, also can be used as anionic inorganic colloid of the present invention such as European patent EP 491879 and the silicon sol described in the EP 502089, these patents are incorporated herein for reference.
For producing the flocculating biosolids, the anionic inorganic colloid of significant quantity be used with organic polymer.The scope of significant quantity can be SiO 2And so on solids content be about 1/1000000th～7500 (ppm) of current solution weight.Preferable range is about 1～5000 ppm, depends on concrete anionic inorganic colloid.For selected anionic inorganic colloid, preferable range is as follows: for poly-silicic acid or poly-silicic acid microgel, be 2～500 ppm; For colloid silica, be 4～1000 ppm; And for mineral colloid soil, as wilkinite, be 2～2000 ppm.Organic polymer
The organic polymer that is applicable to the inventive method comprises cationic polymers and amphiphilic polymers and their mixture.The number-average molecular weight of described organic polymer is generally all greater than 1,000, and 000.These generally are called " high-molecular weight polymer ".
The high molecular weight cation organic polymer comprises cationic starch, cationic guar gum, chitosan and high molecular synthetic cationic polymers, as cationic polyacrylamide.Cationic starch comprises the formed starch of method that reacts and produce the positively charged ion product by starch and tertiary amine or quaternary amine, and substitution value is 0.01～1.0, contains the nitrogen of 0.01～1.0 weight % that has an appointment.The starch that is suitable for comprises potato, corn, wax shape corn, wheat, rice and oat.Preferred high molecular weight cation organic polymer is a polyacrylamide.
The high molecular weight cation organic polymer of significant quantity to be used with anionic inorganic colloid for producing the flocculating biosolids.The scope of cationic polymers significant quantity can be about 0.2～5000ppm of current solution weight.Preferable range is about 1～2500 ppm.
Amphiphilic polymers comprises amphoteric starch, guar gum and synthetic Amphiphatic high polymer amount organic polymer.The consumption of amphiphilic polymers is general identical with the consumption of high-molecular cationic polymer.
The present invention also comprises a kind of method, and it comprises allows the current of the biosolids that comprises the belt surface anionic sites in number contact with first organic polymer of significant quantity, to reduce the number in surface negative charge site.Described first organic polymer is a cationic polymers, and it is used for reducing the number in surface negative charge site and some positively charged ion sites are provided.During its significant quantity is generally and is enough to and on the biosolids at least 1%, the amount in preferred at least 10% surface negative charge site.Lower molecular weight or high molecular weight cation organic polymer or their mixture are all available.Preferred low molecular weight cationic organic polymer is because they have higher cationic degree and lower use cost.
The high-molecular cationic polymer that is suitable for comprise foregoing those.
The molecular weight ranges of the low molecular weight cationic polymkeric substance that is suitable for is about 2,000～about 1,000,000, preferred 10,000～500,000.Low-molecular weight polymer can be, the for example multipolymer of the multipolymer of multipolymer, acrylamide and the diallyl aminoalkyl methacrylic ester of polymine, polyamine, paracyanogen base diamide yuban, amphiphilic polymers, diallyldimethylammonium chloride polymkeric substance, diallyl aminoalkyl methacrylate polymers and dialkyl amino alkyl methyl acrylamide polymer, acrylamide and diallyldimethylammonium chloride, acrylamide and dialkyl group diamino alkyl methyl acrylamide, and the polymkeric substance of dimethyl amine and Epicholorohydrin.These polymkeric substance are at United States Patent (USP) 4,795, describe to some extent in 531 and 5,126,014.
First organic polymer that adds significant quantity, i.e. high molecular or low molecular weight cationic organic polymer or their mixture are to reduce the number of anionic sites in number on the biosolids.Significant quantity depends on Several Factors, comprises the number of biosolids upper surface anionic sites in number in the current, the type of biosolids and the pH value of current.Significant quantity can be used method known to those skilled in the art, utilizes and determines as the technology of colloidal titration and so on.This amount be generally the current gross weight about 0.01～about 10,000ppm.Term " ppm " defines in front.
Current are handled with second organic polymer after first organic polymer is handled again.Described second organic polymer will depend on anionic inorganic colloid.For any anionic inorganic colloid, second organic polymer can be selected from: cationic polymers and amphiphilic polymers and their mixture.When anionic inorganic colloid was the silicon dioxide base anionic inorganic colloid, then second organic polymer can be selected from negatively charged ion, positively charged ion, amphiphilic polymers and their mixture.Positively charged ion and amphiphilic polymers can be high molecular or low-molecular weight polymer as previously mentioned.
The number-average molecular weight that can be used for the anionic polymer of the inventive method is at least 500,000, and the negatively charged ion substitution value is at least 1mol%.Preferred number average molecular weight is greater than 1,000,000 anionic polymer.The preferred anionic substitution value is 10～70mol%.
The example of the anionic polymer that is suitable for comprises the water-soluble ethylene based polyalcohol that contains acrylamide, vinylformic acid, acrylamido-2-sulfonic acid first propyl ester and/or their mixture, also can be hydrolysis acrylamide polymer or acrylamide or homologue, as Methacrylamide and vinylformic acid or homologue, as methacrylic acid, perhaps even with toxilic acid, methylene-succinic acid, vinyl sulfonic acid, acrylamido-2-sulfonic acid first propyl ester and other contain the multipolymer of sulphonate monomer etc.Anionic polymer is at for example United States Patent (USP) 4,643,801; 4,795,531; With 5,126, further description is arranged in 014.
Other can with anionic polymer comprise anionic starch, negatively charged ion guar gum and negatively charged ion polyvinyl acetate (PVA).Optional components
If wish, can drop to below 7 with the pH value of acid earlier current.The general preferred mineral acid of using is as sulfuric acid, hydrochloric acid and nitric acid.Other acid that is suitable for includes, but is not limited to carbonic acid, sulfonic acid and organic acid such as carboxylic acid, vinylformic acid and acidic anionic mineral colloid, one or more protons is arranged by the part neutral acid of metal ion or ammonium ion replacement, and their mixture.The acidic anionic mineral colloid includes, but is not limited to the poly-silicic acid of lower molecular weight, high-molecular-weight poly silicic acid microgel, acid poly-silico-aluminate and sour stabilization polysilicate microgels.At United States Patent (USP) 5,127, the example of sour stabilization polysilicate microgels has been described in 994 and 5,626,721.
Metal-salt can randomly be used for method of the present invention.Iron and aluminium are particularly useful.Acid metal salt can be used to reduce the pH value and plays electric charge and give body.Technology
Method of the present invention relates to and contains biosolids, and as the processing of proteinic current, purpose is to reduce suspended solids (with turbidity measurement) and can optionally isolate biosolids.Biosolids can be through reclaiming for using subsequently.Should be understood that present method both can collect the suspended biological solid and also can collect soluble substance, as be present in those materials in blood and the sugar.
Method of the present invention relates to by allowing current contact with organic polymer with anionic inorganic colloid handles the current that comprise biosolids.This current can come from the technology of this current of any generation, as come from animal or vegetables processing, comprise the processing of non-food use.Described organic polymer is selected from following one group: number-average molecular weight is greater than 1,000,000 cationic polymers and amphiphilic polymers and their mixture.Can optionally allow this current contact, so that the pH value of these current drops to below 7 with acid.In addition, can optionally add metal-salt, particularly molysite or aluminium salt.These reagent, anionic inorganic colloid, organic polymer and acid that can add and/or metal-salt can contact with current by any order, perhaps allow one or more whiles contact with current.In a specific embodiments, current are contact acid and anionic inorganic colloid simultaneously.
Will be optionally the pH value of current be dropped to below 7, can realize that the example of acid as mentioned above with any acid.When the pH value of current being dropped to 7 when following, need not other acid or anionic inorganic colloid source and just can make biosolids flocculating in the current with the acidic anionic mineral colloid.
Allow current contact anionic inorganic colloid and organic polymer.Before this step can drop to below 7 in the pH value with current, carry out afterwards or simultaneously, if wish the step that has one to reduce the pH value.Mineral colloid can or contact with current with any order difference with organic polymer simultaneously.The combination results flocculating biosolids that anionic inorganic colloid and organic polymer contact with current.
The flocculating biosolids can optionally be used traditional partition method, separates from processed current as the combination of sedimentation, floating, filtration, centrifugal, decantation or these methods.The biosolids of separating can be reclaimed and is used for many fields then.Be surprised to find that already that its stink was less than by adopting iron(ic) chloride as the stink in the biosolids that method reclaimed of part flocculation system when the biosolids that is reclaimed by this method was dry.
Generally believe, be suspended in the biosolids in the current,, have surface negative charge as protein.The present invention also provides a kind of method, and it comprises allows the current that contain biological order body contact with first organic polymer of significant quantity, to reduce the number of suspended biological solid upper surface anionic sites in number in the current.Described first polymkeric substance is a cationic polymers, and its consumption will be enough to provide some positively charged ion sites to biosolids.During the general cationic polymers that adds will be enough to and on the biosolids at least 1%, preferred at least 10% surface negative charge.Described first organic polymer can be high molecular or low molecular weight cationic organic polymer.The preferred cationic polymkeric substance is the low molecular weight cationic polymkeric substance.
Current with before first organic polymer contacts, afterwards or simultaneously, allow its contact anionic inorganic colloid and second polymkeric substance, so that in current, produce the flocculating biosolids.Described second organic polymer is selected from positively charged ion, both sexes and anionic polymer and their mixture, and which kind of adds, and depends on anionic inorganic colloid.For any anionic inorganic colloid, second organic polymer can be selected from positively charged ion and amphiphilic polymers and their mixture.For the silicon dioxide base anionic inorganic colloid, second organic polymer can be selected from negatively charged ion, positively charged ion, amphiphilic polymers and their mixture.
The flocculating biosolids can be used known technology, and technology is as previously mentioned separated and reclaimed.
EXAMPLE Example 1
From the washing water sample that Eastern Shore bird source mill obtains, the not flocculating that contains the 1000ppm that has an appointment contains the protein biosolids.Its initial turbidity＞200.Initial pH value is about 7.
In handling, all each times all following reagent is added a beaker: the high molecular weight cation polyacrylamide Percol182  that Switzerland Basel CibaSpecialty Chemicals company produces, 8ppm; Wilmington, DE, the silicon-dioxide microgel solution that E.I.Du Pont Company produces, Particol  MX, 120ppm is (with SiO 2Meter).Shown amount is a benchmark in wash water solution weight.
The adition process of reagent is as follows:
(1) on a Fisher Scientific Model#120MR magnetic stirring apparatus, stir the 250ml washing water with the moderate speed, agitator is the product of Pittsburgh Fisher Scientific company.Add dilute sodium hydroxide or sulfuric acid, the pH value of washing water is adjusted to the value shown in the table 1.
(2) constantly=0 o'clock, add cationic polyacrylamide.
(3) constantly=1 minute the time, add the silicon-dioxide microgel.
(4) constantly=2 minutes the time, agitator speed is kept at a slow speed.
(5) constantly=4 minutes the time, stop to stir, allow the flocculating solid precipitation to beaker bottom.
(6) constantly=10 minutes the time, measure the turbidity of washing water with a Hach ratio turbidometer, as the indication of clarification of water with recovery protein ability, turbidometer is NTU, Laveland, CO, the product of Hach company with this.
(7) constantly=20 minutes the time, add second part of polyacrylamide of 8ppm, and agitator be transferred to the moderate speed.
(8) constantly=21 minutes the time, agitator speed is reduced at a slow speed, and in the time of 23 minutes, stops to stir.
(9) constantly=30 minutes the time, measure turbidity.
Table 1
The test sequence number Washing water pH Turbidity
10 minutes 30 minutes
????1 ????8.0 ????88 ????63
????2 ????6.9 ????79 ????55
????3 ????6.5 ????77 ????42
????4 ????5.5 ????25 ????2
????5 ????4.5 ????30 ????1
????6 ????3.5 ????10 ????2
As by table 1 as seen, turbidity reduces with the adding of cationic polymers and silicon-dioxide microgel.When lower pH value, observe extraordinary result.Turbidity is improved with the adding second time of polyacrylamide, and best result appears at the pH value once more and is lower than at 7 o'clock.
Embodiment 2
With the processing of the bird among the embodiment 1 washing water and different anionic inorganic colloids.Used anionic inorganic colloid is as follows: Ludox  SM colloid silica, the silicon sol of 30 weight %, specific surface area=300m 2/ g.Ludox  HS-30 colloid silica, the silicon sol of 30 weight %, specific surface area=230m 2/ g.Ludox  130 colloid silicas, the silicon sol of 30 weight %, specific surface area=130m 2/ g.Ludox  colloid silica is Wilmington, DE, the product of E.I.Du Pont Company.BMA-670, low " S " value colloidal state silicon sol, specific surface area=850m 2/ g, Sweden Bohus, the product of Eka Chemicals AB company.The colloidal state silicon sol, 4nm, specific surface area=750m 2/ g, Naperville, Ill, the product of Nalco chemical company.Particol  MX, polysilicate microgels, specific surface area=1200m 2/ g, E.I.Du Pont Company's product.
The high molecular weight cation organic polymer is Percol 182 .
All processing are all carried out according to the following steps:
Stir with the moderate speed in (1) beaker,, the pH value of the bird processing washing water of 250ml embodiment 1 wherein is adjusted to 4.5 simultaneously by adding dilute sulphuric acid.
(2) constantly=0 o'clock, add SiO 2With respect to wash water solution weight is the anionic inorganic colloid of 40ppm.
(3) constantly=1 minute the time, add the high molecular weight cation organic polymer of 4ppm.
(4) constantly=2 minutes the time, agitator speed is reduced to deep low gear.
(5) constantly=4 minutes the time, close magnetic stirring apparatus.
(6) constantly=10 minutes the time, measure the turbidity of the washing water on the flocculating solid.
Table 2
Colloid Turbidity in the time of 10 minutes
????Ludox SM ????15
????Ludox HS-30 ????24
????Ludox 130 ????28
????BMA-670 ????11
????Nalco?SiO 2Colloidal sol ????11
????Patticol MX ????2.5
As seen by table 2, can use different anionic inorganic colloids, they are all effective to the turbidity that reduction contains the protein washing water.The flocculating biosolids is deposited to beaker bottom from water.
Embodiment 3-8
In these embodiments, adopt second bird processing washing water that contain the 1390ppm biosolids of having an appointment.Its initial turbidity＞200.Amount in the according to the form below shown in the 3-8 adds following reagent in the washing water: low molecular weight cationic organic polymer, i.e. diallyl ammonio methacrylate polymkeric substance (poly-dadmac); Anionic inorganic colloid; Nalco colloidal state silicon sol Particol , polysilicate microgels and bentonite clay; And high molecular weight cation organic polymer Percol182 , polyacrylamide (PAM).Added amount of reagent is shown in table 3-8.All amounts all are unit with ppm, are benchmark in wash water solution weight.
Embodiment 3 (contrast)
Stir the 250ml washing water with the moderate speed.Constantly=0 o'clock, add poly-dadmac.Constantly=10 seconds the time, add anionic inorganic colloid.After 15 seconds, stop to mix and washing water are transferred in the air-floating apparatus that the 300ml beaker of high form arranged, be equipped with the frited glass separator (diameter 30mn, medium porosity) that is positioned at the beaker center on the beaker.
At 1 pound/inch 2With about 50ml/ minute speed washing water are advanced in air spray under the pressure, up to constantly=stop air spray 4 minutes the time.Write down 5 minutes with 10 minutes turbidity constantly.
Table 3
The test sequence number Poly-dadnac Colloid Turbidity
????ppm Nalco solvent SiO 2,ppm ?Partcol MX ?SiO 2,ppm 5 minutes 10 minutes
??1 ????10 ????20 ??＞200 ??＞200
??2 ????10 ????40 ??＞200 ??＞200
??3 ????10 ????20 ??＞200 ??＞200
??4 ????10 ????40 ??＞200 ????129
??5 ????16 ????20 ??＞200 ??＞200
??6 ????16 ????40 ??＞200 ??＞200
??7 ????16 ????20 ??＞200 ??＞200
??8 ????16 ????40 ??＞200 ????112
As by table 3 as seen, the combination of low molecular weight cationic organic polymer and anionic colloid is not enough to turbidity is dropped to a kind of degree of clarifying washing water that provides.1,2, in 5 and No. 6 tests, do not form throw out.3,4, in 7 and No. 8 tests, formed a kind of finely divided throw out that contains protein solid, but this throw out can't be separated from washing water.
Embodiment 4
Adopt with embodiment 3 in identical method, but after adding anionic inorganic colloid, during 10 seconds, increased the step of an adding high molecular weight cation organic polymer polyacrylamide.After adding for 15 seconds, polyacrylamide stops to mix.Table 4 has provided the amount of reagent and the result that add.
Table 4
The test sequence number Poly-dadmac Colloid PAM Turbidity
????ppm Nalco colloidal sol ppm, SiO 2 ?Partcol MX ??ppm,SiO 2 ?ppm 5 minutes 10 minutes
????9 ????10 ????20 ????6 ?＞200 ??66
????10 ????10 ????40 ????6 ?＞200 ??57
????11 ????10 ????20 ????6 ???65 ??32
????12 ????10 ????40 ????6 ???38 ??19
????13 ????16 ????20 ????6 ?＞200 ??＞200
????14 ????16 ????40 ????6 ???185 ??82
????15 ????16 ????20 ????6 ???120 ??44
????16 ????16 ????40 ????6 ???15 ??12
As seen by table 4, in the combination of low molecular weight cationic polymkeric substance and anionic inorganic colloid, add high-molecular cationic polymer, improved washing water clarification degree because of having reduced turbidity.9,10, in 11,12,15 and No. 16 experiments, formed the throw out that is located away from washing water top and/or bottom in a large number.This throw out can reclaim.In No. 13 were handled, when the add-on of the poly-dadmac of positively charged ion was big, therefore the anionic sites in number that the anionic inorganic colloid that is added is failed to neutralize and existed on the abundant solid surface had a large amount of solids to be retained in the suspension, so the turbidity height.
Embodiment 5 (contrast)
Make anionic inorganic colloid with wilkinite, repeat the method for embodiment 3.Table 5 has provided added amount of reagent and result.
Table 5
The test sequence number Poly-dadmac Wilkinite Turbidity
????ppm ?ppm,SiO 2 5 minutes 10 minutes
????17 ????10 ????100 ??＞200 ??＞200
????18 ????10 ????200 ??＞200 ??＞200
????19 ????16 ????100 ??＞200 ??＞200
????20 ????16 ????200 ??＞200 ??＞200
As seen,, be not enough to reduce turbidity and provide clarifying washing water low molecular weight cationic polymkeric substance and wilkinite combination as anionic inorganic colloid by table 5.What form is to disperse very thin throw out, can't separate from washing water.
Embodiment 6
The employing bentonite clay is an anionic inorganic colloid, repeats the method for embodiment 5.Table 6 has provided amount of reagent and the result who is added.
Table 6
The test sequence number Poly-dadmac Wilkinite ??PAM Turbidity
????ppm ?ppm,SiO 2 ??ppm 5 minutes 10 minutes
??21 ????10 ????100 ????6 ??＞200 ????147
??22 ????10 ????200 ????6 ????84 ????46
??23 ????16 ????100 ????6 ??＞200 ??＞200
??24 ????16 ????200 ????6 ????158 ????77
As seen, in the bentonitic combination, adding high-molecular cationic polymer, because of reducing the clarity that turbidity has improved washing water with the low molecular weight cationic polymkeric substance and as anionic inorganic colloid by table 6.In 21 and No. 23 are handled, formed finely divided throw out, the wilkinite quantity not sufficient that is wherein added is with the existing a large amount of cationic charge that neutralizes.In these were handled, solid failed to separate well.In 22 and No. 24 tests, formed the throw out that is located away from the washing water top and bottom in a large number.
Embodiment 7
Stir the 250ml washing water with the moderate speed, add dilute sulphuric acid and make the pH value reduce to 3.5.Constantly=0 o'clock, add anionic inorganic colloid.Constantly=10 seconds the time, add high molecular weight cation polyacrylamide.After 15 seconds, stop to mix and washing water being transferred in the air-floating apparatus described in the comparative example 3.At 1 pound/inch 2Pressure under with 50ml/ minute speed washing water are advanced in air spray, up to constantly=4 minutes the time, stop air spray.Record turbidity when 5 minutes and 10 minutes.
Table 7
Sequence number Colloid, ppm, SiO 2 PAM Turbidity
Nalco colloidal sol Particol MX Wilkinite ppm 5 minutes 10 minutes
??25 ????20 ??6 ????163 ????151
??26 ????40 ??6 ????136 ????125
??27 ????20 ??6 ????29 ????17
??28 ????40 ??6 ????12 ????10
??29 ????100 ??6 ??＞200 ????131
??30 ????200 ??6 ????90 ????38
As seen by table 7, add anionic inorganic colloid and high molecular weight cation organic polymer then by the pH value that reduces washing water earlier, just reduced turbidity.In table in listed all Processing Test, formed be located away from washing water top and/or bottom by thin to the big closely knit throw out that contains solid protein matter.This protein that contains flocculates and can reclaim.Implement 8
Stir 250ml bird processing washing water with the moderate speed.Add dilute sulphuric acid its pH value is reduced to 3.5.Constantly=0 o'clock, add polysilicate microgels Patticlo  MX.Constantly=20 seconds the time, add high molecular weight cation polyacrylamide (PAM).Constantly=30 seconds the time, stop to mix and washing water being transferred in the air-floating apparatus described in the comparative example 3.Under the pressure of 1 pound/in2, washing water are advanced in air spray with 100ml/ minute speed, up to constantly=stop air spray 4 minutes the time.Record turbidity when 5 minutes and 10 minutes.Then constantly=liquid is discharged through screen cloth from air-floating apparatus 12 minutes the time, and measure the turbidity of liquid effluent.Containing protein solid is collected on screen cloth.
Table 8
The test sequence number Particol MX ??ppm,SiO 2 ??PAM ??ppm Turbidity
5 minutes 10 minutes Liquid effluent
??31 ????20 ????6 ????51 ????30 ????28
??32 ????40 ????6 ????14 ????10 ????13
As by table 8 as seen, the turbidity of washing water constantly reduces in time.And this embodiment has demonstrated the solid collection has been realized the separation of solid from washings at screen cloth.The turbidity of liquid effluent is compared with 10 minutes value, changes very for a short time, illustrates that after this processing neutralizing treatment, solid has been stayed on the screen cloth, can not disperse again.
Embodiment 9
Source mill has obtained another washing water sample from Eastern Shore bird, and it contains the not flocculating biosolids of the 1000ppm that has an appointment, and turbidity surpasses 200.
Make polysilicate microgels solution Particol  MX stable with sulfuric acid.Allow the different time of this microgel ageing of solution before use earlier, digestion time is as shown in table 9.
Stir the 250ml washing water with the moderate speed.Constantly=0 o'clock, adding with respect to washing water weight is high molecular weight polyacrylamide Percol 182  of 8ppm.Constantly=and 1 minute the time, adding ageing polysilicate microgels solution through sour stabilization, add-on is the 120ppm of wash water solution weight.Make single test at each digestion time.Constantly=2 minutes the time, stirring velocity is reduced at a slow speed.Constantly=5 minutes the time, stop to stir.Constantly=15 minutes the time, measure the turbidity of washing water.
Table 9
Digestion time Turbidity
15 seconds ??122
5 minutes ??39
15 minutes ??21
45 minutes ??5
As by the result in the table 9 as seen, the combination of a kind of sour stabilization polysilicate microgels and cationic polyacrylamide is enough to reduce the turbidity of washing water, and does not need earlier the pH value to be dropped to below 7.In addition, the result shows, when the polysilicate microgels digestion time is longer, is obtaining further raising aspect the reduction turbidity.In another experiment of being done with similar aged microgel solution, the mean sizes of microgel is increased to the 230nm of digestion time in the time of 45 minutes from the 5nm of digestion time in the time of 15 seconds.
Embodiment 10
With the moderate speed stir 250ml be taken from Protein Technlogies company, contain 0.51% proteinic soya-bean milk solution.The adding dilute sulphuric acid transfers to 2.5 with the pH value of this solution.Constantly=0 o'clock, adding with respect to the soybean solution weight is the BMA-9 colloid silica of 160ppm, and mixes 10 minutes with the moderate speed, BMA-9 is the product of Sweden Bohus EkaChemicals AB company.Add then with respect to the soybean solution weight and be high molecular weight polyacrylamide Percol 182  of 8ppm and mixed 10 minutes.Use Clifton, NJ, the glass filter paper 934AH filtering mixt that Whatman company produces.Reclaim 0.11g solid protein matter.Filtered solution contains 0.416% protein, and the expression protein content has reduced by 20%.
Embodiment 11
In flowing, handles in water the waste water stream that comes from Eastern Shore bird source mill with continuous processing according to the present invention.In this waste water stream, add the pH value that is enough to make current simultaneously and reduce to 3.7 sulfuric acid and SiO 2With respect to the current solution weight is the polysilicate microgels Particol  MX of 95ppm.In the downstream (about 30 seconds) of acid and microgel adding place, adding with respect to the current solution weight is the cationic polyacrylamide Percol182  of 4ppm.Allow these current flow directly in the dissolving air flotation cell (DAF), solid floats to upward surperficial and is stripped from so that reclaim herein.The current that stay are measured chemical oxygen demand (COD) (COD) and biological oxygen demand (BOD) and suspended solids total amount (TSS).
COD measures with a Loveland, the Hach COD Test Kit that CO.Hach company makes.Method 2450 D mensuration in " detecting the standard law of water and waste water " that TSS co-publicates with U.S. public health federation, AWWA and water surrounding federation.BOD measures with the method in " detecting the standard law of water and waste water " 5210.
Table 10
Handle COD,mg/l ?BOD,mg/l ?TSS,mg/l
Be untreated ????2970 ????1393 ????N/T *
Embodiment 11 ????180 ????180 ????67
* N/T=does not test.But its value is generally about 1000mg/l before processing.
As by table 10 as seen, method of the present invention has reduced the chemistry and the biological oxygen demand of the continuous waste water stream of existing bird source mill.
Embodiment 12
Stir the slurry of the unmodified W-Gum Staley of 20g Pearl Starch in 980g water with the moderate speed.Constantly=0 o'clock, with Particol  MX, i.e. the form of the polysilicate microgels solution of sour stabilization adding is the SiO of 10ppm with respect to starch size weight 2, and mixed 15 seconds.Constantly=15 seconds the time, add and be high molecular weight polyacrylamide Percol 182  of 2ppm and mixed for 30 seconds with respect to starch size weight.Stop then mixing.Leave standstill after 30 seconds constantly=to record turbidity 45 seconds the time be 46.Repeat this test, but add the SiO of 20 ppm with the form of Particol  MX 2Turbidity in the time of 45 seconds is 29.In the 3rd simultaneous test, do not add Particol  MX, turbidity is 186.Embodiment 13
Source mill obtains wastewater sample from Eastern Shore bird.COD＞the 2100ppm of this waste water, its initial turbidity＞200, the pH value is 6.1.In a 400ml beaker, pour the described waste water of 250ml into.Stir this waste water with oar propeller blade profile agitator with 276rpm.With rare H2SO4 the pH value of this waste water is adjusted to 5.5.Constantly=0 o'clock, add silicon-dioxide microgel Particol  MX.Constantly=15 seconds the time, add cationic polymers polyacrylamide (PAM), Percol 182 .Constantly=and 25 seconds the time, or polymkeric substance is reduced to 150rpm with mixer speed when adding back 10 seconds.When polymkeric substance adds back 40 seconds, stop to mix.Mix and to stop to measure turbidity from wastewater sampling during with 95 seconds in back 35 seconds.After measuring turbidity in 95 seconds, measure the pH value again.Mixed for 30 seconds with 150rpm then, make the waste water of flocculating become suspension again.After 1 minute, interrupt stirring, get the waste water sample and measure COD.
COD VA available from Calverton, the 0-1500ppm COD colorimetric analysis ampoule of CHEMetrics company and Milton Roy Spectronic 20 type spectrophotometers are set in the 620nm wavelength and measure.Table 11 has provided amount of reagent and the result who adds in 33 and No. 34 tests.
Embodiment 14
Repeat the method for embodiment 13, with identical wastewater sample.But do not add acid, but before adding Particol  MX, add FeCl during 15 seconds 3All time is all than moving for 15 seconds after the time among the embodiment 13.The amount of reagent that adds in No. 35 tests and the results are shown in table 11.
Table 11
The test sequence number Partcol MX ??ppm,SiO 2 Cationic PAM, ppm Turbidity Last pH ?COD ?ppm
????35s ????95s
????33 ????120 ????12 ????33 ????32 ????5.68 ??475
????34 ????80 ????12 ????10 ????9 ????5.63 ??386
????35 ????120 ????12 ????16 ????14 ????5.61 ??415
As by table 11 as seen, the coupling of acid or iron(ic) chloride, silicon-dioxide microgel and cationic polyacrylamide can reduce the turbidity and the chemical oxygen demand (COD) of the waste water stream that contains biosolids effectively.
Embodiment 15
Repeat the method for embodiment 13, with identical wastewater sample.But cancellation reduces the step of pH value and changes organic polymer.Constantly=0 o'clock, add Particol  MX.Constantly=15 seconds, add the low molecular weight cationic polymkeric substance: the polyamine that Ciba Specialty Chemicals company is produced, Agelfloc  A50HV.Constantly=and 30 seconds the time, adding second organic polymer, it is cationic polyacrylamide (PAM) Percol  182, or anionic polyacrylamide (PAM) Pereol  155PG, both also are the products of Ciba SpecialtyChemicals company.Constantly=when 40 seconds or polymkeric substance add back 10 seconds, mixing velocity is reduced to 150rpm.When adding back 40 seconds, polymkeric substance stops to mix.Mixing stopped the back in the time of 35 and 95 seconds, got wastewater sample and measured turbidity.After measuring turbidity in 95 seconds, measure the pH value.Mixing with 150rpm then makes flocculating waste water become suspension again 30 seconds.Interrupt after 1 minute stirring, get wastewater sample and measure COD.Table 12 has provided the amount of reagent and the result that add.
Table 12
The test sequence number Parteol MX ?ppm,SiO 2 Polyamine ppm Cationic PAM ppm Negatively charged ion PAM ppm Turbidity Last pH ?COD ?ppm
?35s ?95s
?36 ?50 ?40 ?12 ?185 ?84 ?6.03 ?444
?37 ?50 ?40 ?12 ?33 ?28 ?5.98 ?429
?38 ?100 ?40 ?12 ?5 ?4 ?5.99 ?415
?39 ?100 ?40 ?12 ?6 ?3 ?5.99 ?540
As seen by table 12, different organic polymer and can be used to clarified wastewater and reduce chemical oxygen demand (COD) with the various combination of anionic colloid.In 36 and No. 38 tests, with low molecular weight cationic polyamine and high molecular weight polyacrylamide combination.In No. 37 and No. 39 are tested, with polyamine and anionic polyacrylamide combination.
Embodiment 16
Repeat the method for embodiment 13, different is to add Particol  MX to add alkali before, and promptly sodium hydroxide brings up to 6.5 to the pH value.The operation of other step is constant.Table 13 has provided the amount of reagent and the result that add.
Table 13
The test sequence number Partcol MX ?ppm,SiO 2 Cationic PAM, ppm Turbidity Last pH ?COD ?ppm
??35s ??95s
?40 ????80 ????12 ??55 ??55 ??6.42 ?766
?41 ????40 ????12 ??34 ??34 ??6.51 ?628
As seen by table 13, adopt anionic colloid and cationic polymers, can be in the pH value near the clarification that realized waste water stream at 7 o'clock and the reduction of chemical oxygen demand (COD) thereof.

Claims (18)

1. one kind makes the liquid stream that contains biosolids, is essentially water contact with the following material of significant quantity:
(a) anionic inorganic colloid; With
(b) organic polymer, wherein, described organic polymer is selected from cationic polymers, amphiphilic polymers and their mixture; Thereby form the method for flocculating biosolids.
2. the method for claim 1 also is included in step (a) before, allows current contact with first organic polymer of significant quantity, and to reduce the anionic sites in number on the biosolids, described first organic polymer is a cationic polymers.
3. claim 1 or 2 method, wherein, the add-on of described anionic inorganic colloid in the aqueous solution is 1～7500ppm of current liquid weight, and the add-on of described organic polymer in current is 0.2～5000ppm of current liquid weight.
4. the method for claim 1,2 or 3, wherein, described anionic inorganic colloid is selected from polysilicate, poly-silico-aluminate, poly-silicic acid microgel and their mixture.
5. the method for claim 4, wherein, the size of described anionic inorganic colloid is greater than 10nm.
6. the method for any one in the claim 1～5, wherein said organic polymer is a cationic polymers.
7. the method for claim 6, wherein said cationic polymers is selected from polyacrylamide, cationic starch, cationic guar gum, chitosan and their mixture.
8. the method for any one in the claim 1～5, wherein, described organic polymer is an amphiphilic polymers.
9. the method for any one in the claim 1～8 also comprises and separates and the described flocculating biosolids of recovery.
10. the method for any one in the claim 1～9 wherein allows described current contact with acid, so that the pH value of these current drops to below 7.
11. the method for claim 10, wherein said acid are selected from sulfuric acid, hydrochloric acid, nitric acid, carbonic acid gas, sulfonic acid, carboxylic acid, vinylformic acid, acidic anionic mineral colloid, the acid of part neutral, and their mixture.
12. the method for claim 10, wherein, described acid is selected from sulfuric acid, hydrochloric acid, nitric acid and their mixture.
13. the method for claim 10, wherein, described acid is to be selected from following one group acidic anionic mineral acid: lower molecular weight is gathered silicic acid, high-molecular-weight poly silicic acid microgel, acid poly-silico-aluminate and sour stabilization polysilicate microgels and their mixture.
14. claim 10,11,12 or 13 method, wherein, described liquid stream is contact acid and anionic inorganic colloid simultaneously.
15. the method for any one in the claim 2～14, wherein, described first organic polymer is that number-average molecular weight is 2,000～1,000,000 low molecular weight cationic polymkeric substance.
16. the method for any one in the claim 2～14, wherein, described first organic polymer be number-average molecular weight greater than 1,000,000 high-molecular cationic polymer.
17. the method for any one in the claim 2～16, wherein, described anionic inorganic colloid is the silicon dioxide base anionic inorganic colloid; And described organic polymer is selected from cationic polymers, anionic polymer and amphiphilic polymers.
18. the method for claim 17, wherein said silicon dioxide base anionic inorganic colloid are selected from colloid silica, polysilicate microgels, poly-silico-aluminate microgel, poly-silicic acid, poly-silicic acid microgel and their mixture of colloid silica, aluminium modification.
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CN101671077B (en) * 2009-09-30 2012-10-17 江苏苏净集团有限公司 Film-forming material on filler for removing nitrogen from wastewater
WO2012142879A1 (en) 2011-04-20 2012-10-26 佛山市优特医疗科技有限公司 Wound dressing with bacteriostasis and hygroscopicity

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