JP3327813B2 - Sludge dewatering method - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

TECHNICAL FIELD The present invention relates to a sludge dewatering agent comprising a crosslinked amphoteric polymer, and a sludge dewatering agent of the present invention is a metal hydroxide generated from a wastewater treatment step pretreated with an inorganic flocculant. It is particularly effective for a sludge dewatering method for dewatering contained sludge.

[0002]

2. Description of the Related Art Various sludge dewatering agents and sludge dewatering methods have been known. For example, a sludge dewatering method in which an amphoteric polymer flocculant is added to an organic sludge having a sludge PH of 5 to 8 after addition of an inorganic flocculant (JP-A-63-15820)
No. 0) is known. Further, in order to improve the drawbacks of the conventional polymer flocculant, a crosslinked cationic / anionic / nonionic organic polymer flocculant (European Patent No. 0,202,780; 61-29
No. 3510, JP-A-64-85199, JP-A-2-219878, JP-A-4-226102, etc.) have been proposed to be effective for various solid-liquid separations. However, the effect of the cross-linked amphoteric organic polymer flocculant is not known, and the cross-linking property is controlled by the coexistence of a chain transfer agent during reverse-phase emulsion polymerization, and the resulting emulsion has a hydrophilic surfactant. An organic polymer flocculant having a practical solubility by adding an agent (phase inversion agent) was also unknown.

[0003]

Conventionally known amphoteric polymers or cationic polymers are unsatisfactory in performance. In particular, the metal hydroxide-containing sludge obtained through a solid-liquid separation step after adding an inorganic coagulant to food wastewater or oil-containing wastewater and performing a coagulation treatment, has a large content of fine particles and is poor in dewaterability, and the sludge is poor. There has been no known amphoteric organic polymer flocculant which is effective for a method of dewatering sludge and exhibits a sufficient effect.

[0004]

The amphoteric organic polymer flocculant used in the sludge dewatering method of the present invention is diluted with water to a concentration to be added to the sludge, and particles having a particle size of 30 μm or less are observed with a microscope. , The diluted solution is applied to a glass plate,
An organic sludge dewatering agent having the property of forming a continuous dry film when dried by heating at ° C. The method for producing such a sludge dewatering agent is as follows. (A) 5 to 97.9999 mol% of all the monomers, a water-soluble cationic vinyl monomer represented by the following formula (1) or a mixture thereof, and (B) 0.0001 to 0 of all the monomers. .01
Mol% bifunctional monomer, (C) 2 to 30 mol% of water-soluble anionic vinyl monomer or a mixture thereof among all monomers, (D) nonionic water-soluble monomer, (E) A chain transfer agent, (F) water, (G) an oil comprising at least one hydrocarbon, and (H) at least one HLB that is an amount effective to produce a reverse phase or water-in-oil emulsion. A surfactant is prepared, and the above (A) to
(H) The components are mixed appropriately and vigorously stirred to form fine monomer phase droplets in the oil phase, and then polymerized, mixed with a hydrophilic surfactant, and diluted with water for use. Features.

Embedded image (Where A is O or NH; B is C ₂ H ₄ , C ₃
H ₆ , C ₃ H ₅ OH; R ₁ is H or CH ₃ ; R ₂ , R
₃ represents an alkyl group having 1 to 4 carbon atoms; R ₄ represents hydrogen or an alkyl group having 1 to 4 carbon atoms or a benzyl group; X ⁻ represents an anionic counter ion. )

[0005] The invention of claim 1 of the present invention provides a metal hydroxide-containing sludge obtained through a solid-liquid separation step after adding an inorganic coagulant to wastewater and subjecting the same to the following [(A) ~
(H) The components were mixed appropriately and vigorously stirred to form fine monomer phase droplets in the oil phase, and then subjected to a polymerization operation and mixed with a hydrophilic surfactant to obtain an amphoteric polymer flocculant. It is a sludge dewatering method characterized by adding and stirring, aggregating the metal hydroxide-containing sludge, and dewatering with a dehydrator. (A) A water-soluble cationic vinyl monomer represented by the following formula (1) or a mixture thereof in an amount of 5 to 97.9999 mol% of all monomers.

(Where A is O or NH; B is C ₂ H
₄ , C ₃ H ₆ , C ₃ H ₅ OH; R ₁ is H or CH ₃ ;
R ₂ and R ₃ are an alkyl group having 1 to 4 carbon atoms; R ₄ is hydrogen or an alkyl group having 1 to 4 carbon atoms or a benzyl group;
^- represents an anionic counterion. (B) 0.0001 to 0.01 mol% of the bifunctional monomer in all monomers. (C) 2 to 30 mol% of a water-soluble anionic vinyl monomer or a mixture thereof in all monomers. (D) Residual nonionic water-soluble monomer. (E) a chain transfer agent. (F) water. (G) an oil comprising at least one hydrocarbon. (H) at least one surfactant that is an HLB with an amount effective to produce a reversed phase emulsion, ie, a water-in-oil emulsion.

The invention of claim 2 of the present invention is characterized in that the inorganic coagulant is one selected from aluminum sulfate, aluminum chloride, polyaluminum chloride, iron sulfate, iron chloride, polyiron or a mixture thereof. A sludge dewatering method according to claim 1.

[0007] The invention of claim 3 of the present invention is the method for dewatering sludge according to claim 1 , wherein the nonionic water-soluble monomer is (meth) acrylamide.

The invention of claim 4 of the present invention is the method for dewatering sludge according to claim 1 , wherein the water-soluble anionic vinyl monomer is (meth) acrylic acid.

The invention according to claim 5 of the present invention is characterized in that the bifunctional monomer is N, N'-methylenebisacrylamide or 2
The sludge dewatering method according to claim 1 , characterized in that it is hydroxypropylidene 1,3 bis [(N acryloylaminopropyl) N, N dimethylammonium chloride].

The invention according to claim 6 of the present invention is the method for dewatering sludge according to claim 1 , wherein the hydrophilic surfactant is a nonionic surfactant having an HLB of 9 to 15.

[0011]

DESCRIPTION OF THE PREFERRED EMBODIMENTS The above formula (1) used in the present invention
Specific examples of the water-soluble cationic vinyl monomer of the component (A) represented by the following formula are dialkylaminoalkyl (meth)
Tertiary and quaternary ammonium salts of acrylate, tertiary and quaternary ammonium salts of dialkylaminoalkyl (meth) acrylamide, tertiary and quaternary ammonium salts of dialkylaminohydroxyalkyl (meth) acrylate, dialkylaminohydroxyalkyl Examples thereof include one selected from tertiary and quaternary ammonium salts of (meth) acrylamide or a mixture thereof. Among them, one selected from acryloyloxyethyltrimethylammonium chloride, methacryloyloxyethyltrimethylammonium chloride, dimethylaminopropylacrylamide hydrochloride or a mixture thereof is preferably used.

Specific examples of the bifunctional monomer (B) used in the present invention include 2-hydroxypropylidene 1,
3-bis [(Nacryloylaminopropyl) N, N-dimethylammonium chloride], N, N'-methylenebisacrylamide, N, N'-methylenebismethacrylamide, divinyl compounds such as divinylbenzene, methylolacrylamide, methylolmethacrylamide, etc. Vinyl methylol compounds, vinyl aldehyde compounds such as acrolein, and mixtures thereof. Among them, 2-hydroxypropylidene 1,1
3bis [(N acryloylaminopropyl) N, N dimethyl ammonium chloride] can be preferably used.
N'-methylenebisacrylamide is second to this.

Specific examples of the water-soluble anionic vinyl monomer (C) used in the present invention include (meth) acrylic acid, 2-acrylamido-2-methylpropanesulfonic acid, vinylsulfonic acid, and styrenesulfonic acid. Acid, itaconic acid, maleic acid, fumaric acid, arylsulfonic acid and salts thereof, or mixtures thereof.
Among these, acrylic acid can be most preferably used.

Specific examples of the water-soluble nonionic vinyl monomer (D) used in the present invention include (meth) acrylamide, vinyl methyl ether, vinyl ethyl ether and mixtures thereof. Among them, acrylamide is most preferably used.

Specific examples of the chain transfer agent of the component (E) used in the present invention include alcohol, mercaptan, phosphite, sulphite and mixtures thereof. The amount of these chain transfer agents added is such that the amphoteric organic polymer flocculant is diluted with water to the concentration to be added to the sludge,
Particles having a particle size of 30 μm or less are observed under a microscope, and the diluent is selected so as to have a property of forming a continuous dried film when applied to a glass plate and dried by heating at 105 ° C.

Specific examples of the oil comprising at least one kind of hydrocarbon which is the component (G) used in the present invention include mineral oils such as kerosene, light oil and medium oil, and boiling points having substantially the same range as these. Examples thereof include hydrocarbon-based synthetic oils having characteristics such as viscosity, and mixtures thereof.

The surfactant (H) used in the present invention is a nonionic surfactant having an HLB of 3 to 6,
Specific examples thereof include sorbitan monooleate, sorbitan monostearate, and sorbitan monopalmitate.

In the present invention, as the hydrophilic surfactant (so-called phase inversion agent) mixed with the polymer obtained by the water-in-oil emulsion polymerization, a cationic surfactant or a nonionic surfactant of HLB 9 to 15 is used. And preferably a nonionic surfactant having an HLB of 10 to 14. Representative examples of preferred nonionic surfactants include, for example, polyoxyethylene nonylphenyl ether.

The amount of the bifunctional monomer of the component (B) used in the present invention, for example, the ratio of N, N'-methylenebisacrylamide to the total amount of the polymerizable monomer is from 0.0001 to 0.0001.
0.01 mol%, preferably 0.0002 to 0.003
It is desirable to copolymerize in the range of mol%. 0.000
If it is less than 1 mol%, a sufficient network structure cannot be obtained, and excellent dehydration performance cannot be obtained. On the other hand, if the amount exceeds 0.01 mol%, a water-insoluble polymer is formed, and even if added to and mixed with sludge, a floc having good dewaterability cannot be obtained.

The polymer according to the present invention can be copolymerized by an essentially known polymerization method. For example, after mixing and emulsifying an aqueous solution containing a polymerizable vinyl monomer and a chain transfer agent and an organic dispersion medium containing a nonionic surfactant having an HLB of 3 to 6, in the presence of a radical polymerization initiator, Temperature 30 ~
A method for producing a water-in-oil cationic polymer emulsion by polymerizing at 80 ° C. is described in JP-A-61-236250, but this method is applied by changing the monomer composition by applying this method. The water-in-oil emulsion of the invention can be synthesized. A hydrophilic surfactant is added to this water-in-oil emulsion, mixed with water, phase-inverted to an oil-in-water emulsion, and used as a dehydrating agent. The conditions for addition to the sludge after dissolution are not different from those of a general amphoteric polymer flocculant.

[0021]

EXAMPLES Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist.

(Synthesis Example 1 of the Present Invention) A reaction vessel equipped with a stirrer and a temperature controller was provided with a boiling point of 190 ° C. to 230 ° C.
120.0 kg of isoparaffin of C and 7.5 kg of sorbitan monooleate were charged. 165 kg of demineralized water
And acryloyloxyethyltrimethylammonium chloride (AMC) 27.9997 mol% (represented as about 28 in Table 1), 2-hydroxypropylidene 1,3 bis [(N acryloylaminopropyl) N, N dimethyl ammonium chloride] ( HPAD) 3 × 10 ^-4 mol%,
A mixture of 200 kg of a monomer having a composition of 70 mol% of acrylamide (AAM) was added, and the mixture was emulsified and stirred with a homogenizer. 200 g of isopropyl alcohol was added to the obtained emulsion, and after purging with nitrogen, 40 g of dimethylazobisisobutyrate was added to complete the polymerization reaction while controlling the temperature at 50 ° C., and then 7.5 kg of polyoxyethylene nonylphenyl ether was added. A sample (sample-1) to be subjected to the test after addition and mixing was used.

(Synthesis Example 2 of the Present Invention) Acryloyloxyethyltrimethylammonium chloride (AMC)
9997 mol% (represented as about 50 in Table 1), acrylic acid (AAC) 10 mol%, 2-hydroxypropylidene 1,
Synthesis Example 1 except that a mixture of 200 kg of a monomer having a composition of 3 bis [(N acryloylaminopropyl) N, N dimethyl ammonium chloride] (HPAD) 3 × 10 ^-4 mol% and acrylamide (AAM) 40 mol% was used. In the same manner as in the above, a sample (sample-2) to be subjected to the test was obtained.

(Synthesis Example 3 of the Present Invention) Acryloyloxyethyltrimethylammonium chloride (AMC)
998 mol% (represented as about 50 in Table 1), acrylic acid (AAC) 10 mol%, 2-hydroxypropylidene 1,
Synthesis Example-1 except that a mixture of 200 kg of a monomer having a composition of 3 bis [(N acryloylaminopropyl) N, N dimethylammonium chloride] (HPAD) 2 × 10 ^-3 mol% and acrylamide (AAM) 40 mol% was used. In the same manner as in the above, a sample (sample-3) to be subjected to the test was obtained.

(Synthesis Example 4 of the Present Invention) Acryloyloxyethyltrimethylammonium chloride (AMC)
Composition of 998 mol% (expressed as about 50 in Table 1), acrylic acid (AAC) 10 mol%, N, N 'methylenebisacrylamide (MBAA) 3 × 10 ^-4 mol%, acrylamide (AAM) 40 mol% A sample to be subjected to the test (Sample-4) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of the monomer was used.

(Synthesis Example 5 of the Present Invention) Acryloyloxyethyltrimethylammonium chloride (AMC)
Composition of 998 mol% (expressed as about 50 in Table 1), acrylic acid (AAC) 10 mol%, N, N 'methylenebisacrylamide (MBAA) 2 × 10 ^-3 mol%, acrylamide (AAM) 40 mol% A sample to be subjected to the test (Sample-5) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of the above monomer was used.

(Comparative Product Synthesis Example-1) Acryloyloxyethyltrimethylammonium chloride (AMC)
9997 mol% (denoted as about 30 in Table 1), 2-hydroxypropylidene 1,3 bis [(N acryloylaminopropyl) N, N dimethyl ammonium chloride] (HP
AD) 3 × 10 ^-4 mol%, acrylamide (AAM) 7
A sample to be subjected to a test (sample-6) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of a monomer having a composition of 0 mol% was used.

(Comparative Product Synthesis Example 2) Acryloyloxyethyltrimethylammonium chloride (AMC) 28 mol% (represented as 28 in Table 1), acrylic acid (AAC) 2 mol% A sample to be subjected to a test (sample-7) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of monomer having a composition of 70 mol% of acrylamide (AAM) was used.

(Comparative product synthesis example-3) Acryloyloxyethyltrimethylammonium chloride (AMC) 50 mol% (indicated as 50 in Table 1), acrylic acid (AAC) 10 mol%, A sample to be subjected to a test (sample-8) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of monomers having a composition of 40 mol% of acrylamide (AAM) was used.

(Comparative Product Synthesis Example 4) Acryloyloxyethyltrimethylammonium chloride (AM) was added without adding isopropyl alcohol as a chain transfer agent.
C) 49.998 mol% (indicated as about 50 in Table 1), acrylic acid (AAC) 10 mol%, 2-hydroxypropylidene 1,3 bis [(N acryloylaminopropyl)
N, N dimethyl ammonium chloride] (HPAD) 2
× 10 ^-3 mol%, acrylamide (AAM) 40 mol%
A sample to be subjected to the test (Sample-9) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of the monomer having the composition described above was used.

(Comparative Product Synthesis Example-5) Acryloyloxyethyltrimethylammonium chloride (AM) was added without adding isopropyl alcohol as a chain transfer agent.
C) 49.998 mol% (indicated as about 50 in Table 1), acrylic acid (AAC) 10 mol%, N, N ′ methylenebisacrylamide (MBAA) 2 × 10 ⁻³ mol%, acrylamide (AAM) 40 200 mole% monomer
A sample to be subjected to the test (Sample-10) was prepared in the same manner as in Synthesis Example 1 except that a mixture of Kg was used.

(Comparative Product Synthesis Example-6) Acryloyloxyethyltrimethylammonium chloride (AMC) 49.998 mol% (Table 1) without adding polyoxyethylene nonylphenyl ether as a phase inversion agent to the polymer.
In about 50), acrylic acid (AAC) 10 mol%, 2-hydroxypropylidene 1,3 bis [(N acryloylaminopropyl) N, N dimethyl ammonium chloride] (HPAD) 2 × 10 ^-3 mol%, A sample to be subjected to a test (sample-11) was prepared in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of monomers having a composition of 40 mol% of acrylamide (AAM) was used.

(Comparative product synthesis example-7) Acryloyloxyethyltrimethylammonium chloride (AMC) 49.998 mol% (Table 1) without adding polyoxyethylene nonylphenyl ether as a phase inversion agent to the polymer.
, Acrylic acid (AAC) 10 mol%, N, N 'methylenebisacrylamide (MBAA)
A sample to be subjected to a test in the same manner as in Synthesis Example 1 except that a mixture of 200 kg of a monomer having a composition of 2 × 10 ⁻³ mol% and acrylamide (AAM) 40 mol% was used (sample 1).
2). The above is summarized in Table 1.

[0034]

[Table 1]

(Observation result-1) Samples 1 to 6 in an emulsion state were mixed with tap water using an actual stirring device (300 rpm).
m), the solution was diluted with stirring to a polymer concentration of 0.2% by weight, and a liquid whose viscosity was increased after 1 hour was collected and observed with a microscope.
μm) were observed, and the diluted solution was applied to a glass plate and dried by heating at 105 ° C. to form a continuous dried film. Further, when the ion equivalent value of this diluted solution was measured by colloid titration, the ion equivalent value was 85% or more of the theoretical value.

(Observation Result-2) In the same manner as in Observation Result-1, Sample-7 to Sample-8 in the emulsion state were diluted with tap water using a real stirring device to a polymer concentration of 0.2% by weight. After 1 hour, the thickened liquid was collected and observed with a microscope. As a result, all of the liquids were homogeneous solutions and no particles were observed. Apply the diluent to a glass plate and apply 105 °
Upon heating and drying at C, a continuous dried film was formed.
Further, when the ion equivalent value of this diluent was measured by colloid titration, all the ion equivalent values were 100% of the theoretical values.

(Observation Result-3) As in Observation Result-1, Samples 9 to 10 in the emulsion state were diluted with tap water using a real stirring device so that the polymer concentration became 0.2% by weight. After 1 hour, the thickened liquid was collected and observed with a microscope. Particles having a particle diameter of 30 μm or less (about 3 μm) were observed on one side, and the diluted liquid was applied to a glass plate and heated to 105 ° C. When heated and dried, a granular discontinuous dried film was formed. Further, when the ion equivalent value of this diluent was measured by colloid titration, all the ion equivalent values were 40% or less of the theoretical values.

(Observation Result-4) As in Observation Result-1, Samples 11 to 12 in an emulsion state were diluted with tap water using a stirrer with an actual machine to a polymer concentration of 0.2% by weight. As a result, the emulsion did not disperse in water, the gel-like mass floated, and a uniform polymer diluent was not obtained. On the other hand, when vigorous stirring was performed with a magnetic stirrer on a beaker scale, the emulsion was dispersed in water, and a uniform polymer diluent was obtained without floating gel-like lumps.

[0039]

EFFECT OF THE INVENTION Observation Results Using the diluent prepared in 1-4, sludge sludge (PH; 7.0, SS;
13300 mg / l, loss on ignition 62.0%, n-Hx;
2300 mg / l, acid-soluble Al ₂ O ₃ ; 3300 mg /
In l), a polymer of 1.2% of SS was added, and the mixture was stirred in a flocculation tank, and the flocculated sludge obtained by flocculating the sludge was dehydrated by a belt press. Table 2 shows the results. The superiority of the product of the present invention is clear.

[0040]

[Table 2]

Embedded image

[Table-1]

[Table-2]

────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-10-244300 (JP, A) JP-A-9-225499 (JP, A) JP-A-9-99599 (JP, A) JP-A-10- 137800 (JP, A) JP-A-10-137799 (JP, A) JP-A-10-137798 (JP, A) JP-A-10-137797 (JP, A) JP-A-9-174100 (JP, A) JP-A-8-300000 (JP, A) (58) Fields investigated (Int. Cl. ⁷ , DB name) B01D 21/01 C02F 11/00-11/20 C02F 1/52-1/56

Claims (6)

(57) [Claims] 1. An inorganic coagulant is added to waste water to perform coagulation treatment, and then the following components (A) to (H) are mixed with the metal hydroxide-containing sludge obtained through a solid-liquid separation step at appropriate times. Vigorous stirring was performed to form fine monomer phase droplets in the oil phase, and then polymerization was performed, followed by mixing with a hydrophilic surfactant.) Amphoteric polymer flocculant was added and stirred. A sludge dewatering method characterized by coagulating oxide-containing sludge and dewatering with a dehydrator. Embedded image (Where A is O or NH; B is C2 H4, C3
H6, C3 H5 OH; R1 is H or CH3; R2, R3
Is an alkyl group having 1 to 4 carbon atoms; R4 is hydrogen or an alkyl group having 1 to 4 carbon atoms or a benzyl group; and X- is an anionic counter ion. (A) A water-soluble cationic vinyl monomer represented by the following formula (1) or a mixture thereof in an amount of 5 to 97.9999 mol% of all monomers. (B) 0.0001 to 0.01 mol% of bifunctional monomers in all monomers. (C) 2 to 30 mol% of a water-soluble anionic vinyl monomer or a mixture thereof in all monomers. (D) Residual nonionic water-soluble monomer. (E) a chain transfer agent. (F) water. (G) an oil comprising at least one hydrocarbon. (H) at least one surfactant that is an HLB with an amount effective to produce a reversed phase emulsion, ie, a water-in-oil emulsion. 2. An inorganic coagulant comprising aluminum sulfate, aluminum chloride, polyaluminum chloride, iron sulfate, iron chloride,
The sludge dewatering method according to claim 1, wherein the sludge is a kind selected from polyiron or a mixture thereof. 3. The method for dewatering sludge according to claim 1 , wherein the nonionic water-soluble monomer is (meth) acrylamide. 4. The sludge dewatering method according to claim 1 , wherein the water-soluble anionic vinyl monomer is (meth) acrylic acid. 5. The method according to claim 1, wherein the bifunctional monomer is N, N'-methylenebisacrylamide or 2-hydroxypropylidene-1,3bis [(Nacryloylaminopropyl) N, N
Sludge dewatering process according to claim 1, characterized in that the dimethylammonium chloride]. 6. The sludge dewatering method according to claim 1 , wherein the hydrophilic surfactant is a nonionic surfactant having an HLB of 9 to 15.