CN106179498A - Polystyrene catalysis bead and slurry photocatalytic reactor - Google Patents

Polystyrene catalysis bead and slurry photocatalytic reactor Download PDF

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Publication number
CN106179498A
CN106179498A CN201610547242.1A CN201610547242A CN106179498A CN 106179498 A CN106179498 A CN 106179498A CN 201610547242 A CN201610547242 A CN 201610547242A CN 106179498 A CN106179498 A CN 106179498A
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CN
China
Prior art keywords
polystyrene
bead
catalysis
acid
light transmission
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Pending
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CN201610547242.1A
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Chinese (zh)
Inventor
孟建强
马六甲
潘赢
张宇峰
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Tianjin Polytechnic University
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Tianjin Polytechnic University
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Priority to CN201610547242.1A priority Critical patent/CN106179498A/en
Publication of CN106179498A publication Critical patent/CN106179498A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/06Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
    • B01J35/39
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/308Dyes; Colorants; Fluorescent agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/10Photocatalysts

Abstract

The invention discloses polystyrene catalysis bead and slurry photocatalytic reactor, polystyrene catalysis bead, make by following method: (1) carries out pretreatment to polystyrene sphere;(2) by pretreatment polystyrene sphere, being dipped in the toluene solution of benzophenone, taking-up is dried, logical nitrogen, irradiates, take out, put in the methanol solution of ionic liquid under ultra-violet lamp, under nitrogen protection, and reaction;Clean, dry, obtain polystyrene graft modification bead;(3) putting in heteropoly acid aqueous solution by polystyrene graft modification bead, lucifuge is reacted, and washes under room temperature, and vacuum lyophilization obtains polystyrene catalysis bead.The polystyrene catalysis bead of the present invention, is immobilized on polystyrene surface by catalyst, in use, is avoided that catalyst loss.The slurry photocatalytic reactor of the present invention runs at normal temperatures, low power consuming, and environmental protection is simple to operate.

Description

Polystyrene catalysis bead and slurry photocatalytic reactor
Technical field
The invention belongs to water treatment field, be specifically related to a kind of can continuous degradation waste water from dyestuff polystyrene catalysis bead And slurry photocatalytic reactor.
Background technology
Along with fast development and the growth in the living standard of human industry's technology, substantial amounts of industrial wastewater and sanitary wastewater quilt It is directly discharged in natural environment, environment is caused serious pollution, the among these directly discharge of a large amount of chemical dyestuff waste water Harm to environment is particularly acute.Pollute especially chemical dyestuff contaminated wastewater to tackle the most serious water, alleviate water danger The significant problems such as machine, exploitation green, the dye wastewater treatment technology of environmental protection become the key subjects of facing mankind.
At present, with one of visible light catalytic dye wastewater degradation focus becoming Recent study, this technology has efficiently, Quickly feature, is that the following mankind solve one of waste water from dyestuff the most promising high-tech technology of pollution.But, directly add Photocatalyst for degrading waste water from dyestuff not only consumption is big but also catalyst is difficult to reclaim, and causes the pollution to environment, causes simultaneously and urge A large amount of wastes of agent.
Summary of the invention
It is an object of the invention to the deficiency directly adding photocatalyst for degrading waste water from dyestuff overcoming prior art to exist, carry For a kind of polystyrene catalysis bead.
Second object of the present invention be to provide one can continuous degradation waste water from dyestuff, directly filter separating catalyst, solve The certainly slurry photocatalytic reactor of a difficult problem for catalyst loss in photocatalytic degradation.
Technical scheme is summarized as follows:
A kind of polystyrene catalysis bead, makes by following method:
1) polystyrene sphere is carried out pretreatment: successively with dehydrated alcohol, deionized water, 2-10% inorganic base water-soluble Liquid, the inorganic acid aqueous solution of 2-10% clean polystyrene sphere, are washed with deionized water to neutrality, vacuum lyophilization, obtain Pretreatment polystyrene sphere;
(2) preparation of polystyrene graft modification bead: pretreatment polystyrene sphere step (1) obtained, is dipped in 5-30min in the toluene solution of 5-25mM benzophenone or the n-heptane solution of 5-25mM benzophenone, takes out and dries in atmosphere, Be placed in hermetic container logical nitrogen 5-180min, then at wavelength be 254-365nm, power be 4-12W ultra-violet lamp under, irradiate Distance is 5-20cm, irradiates 5-30min, takes out, in the methanol solution of the ionic liquid putting into 0.1-0.5M, under nitrogen protection, At 55-65 DEG C, react 12-48h;Successively with deionized water, washes of absolute alcohol, vacuum freezing drying, ionic liquid is poly- Styrene bead surface forms poly ion liquid, obtains polystyrene graft modification bead;The polyphenyl second that described step (1) obtains Alkene bead is 1g:20-30mL with the ratio of the methanol solution of ionic liquid;
(3) in proportion the polystyrene graft modification bead that 1g step (2) obtains is put into the 10-25mM's of 10-100mL In heteropoly acid aqueous solution, under the conditions of lucifuge, water-bath 12-48h at 15-35 DEG C, wash 12-48h under room temperature, vacuum freezing is done Dry that polystyrene is catalyzed bead.
Preferably: described inorganic base is sodium hydroxide or potassium hydroxide.
Described mineral acid is hydrochloric acid or sulphuric acid.
Described ionic liquid is 1-(4-vinyl benzyl)-3-Methylimidazole. villaumite, 1-(4-vinyl benzyl)-3-butyl Imidazoles villaumite, 1-(4 vinyl benzyl)-3-Methylimidazole. bromide or 1-(4-vinyl benzyl)-3-1-Butyl-1H-imidazole smelling salts.
Described heteropoly acid is: phosphomolybdic acid, phosphotungstic acid or silicomolybdic acid.
Slurry photocatalytic reactor includes light transmission container 10, is provided with aeration head 7, is arranged on printing opacity in light transmission container Aeration pump 5 outside container is connected with gas flowmeter 6 and aeration head 7 successively by pipeline;It is provided with the feed pipe of the 1st valve 2 One end is connected with feed pump 1, and the other end is arranged in light transmission container 10, is outside equipped with daylight lamp 8 at light transmission container 10, at printing opacity Flat polyvinylidene fluoride micro-filtration membrane original paper 9 and above-mentioned polystyrene catalysis bead 11, Kynoar it is additionally provided with in container 10 Flat micro-filtration original paper 9 is connected with the 2nd valve 3 being arranged on outside light transmission container 10 and discharging pump 4 successively by pipeline.
Slurry photocatalytic reactor the most according to claim 6, is characterized in that the material of described light transmission container is Glass or polymethyl methacrylate.
Advantages of the present invention:
The polystyrene catalysis bead of the present invention, with polystyrene as substrate, is immobilized on catalyst its surface, is using Time, the problem being avoided that the catalyst loss occurred in traditional method.The slurry photocatalytic reactor of the present invention is at normal temperatures Running, low power consuming, environmental protection, simple to operate, what easy scale was applicable to that following infant industry produces can continuous degradation dyestuff The Technology of waste water.
The slurry photocatalytic reactor of the present invention is more stable during running degraded Acid Orange II molecule continuously, This is important in actual commercial Application.
Accompanying drawing explanation
Fig. 1 is slurry photocatalytic reactor structural representation.
Fig. 2 is the ATR-IR infrared spectrum of polystyrene sphere and modified bead, wherein:
A is the ATR-IR infrared spectrum of polystyrene sphere;
B is the ATR-IR infrared spectrum of polystyrene graft modification bead;
C is the ATR-IR infrared spectrum of polystyrene catalysis bead.
Detailed description of the invention
Be will assist in by following example and understand the present invention, but be not limiting as present disclosure.In addition, it is to be understood that After having read the content that the present invention lectures, the present invention can be made various changes or modifications by those skilled in the art, these etc. Valency form falls within the scope of following claims equally.
Below by embodiment and accompanying drawing, the invention will be further described.
Embodiment 1
A kind of polystyrene catalysis bead, makes by following method:
(1) polystyrene sphere is carried out pretreatment: successively with dehydrated alcohol, deionized water, 5% sodium hydroxide water-soluble Liquid, the aqueous hydrochloric acid solution of 5% clean polystyrene sphere, are washed with deionized water to neutrality, vacuum lyophilization, obtain pretreatment Polystyrene sphere;
(2) preparation of polystyrene graft modification bead: pretreatment polystyrene sphere step (1) obtained, is dipped in 15min in the toluene solution of 15mM benzophenone, takes out and dries in atmosphere, is placed in hermetic container logical nitrogen 90min, then at Wavelength is 365nm, power is under 8W ultra-violet lamp, and irradiation distance is 10cm, irradiates 10min, takes out, puts into the ionic liquid of 0.3M In the methanol solution of body, under nitrogen protection, at 60 DEG C, react 36h;Successively with deionized water, washes of absolute alcohol, vacuum is cold Freezing drying, ionic liquid forms poly ion liquid on polystyrene sphere surface, obtains polystyrene graft modification bead;Described The polystyrene sphere that step (1) obtains is 1g:25mL with the ratio of the methanol solution of ionic liquid;
The ionic liquid of the present embodiment is: 1-(4-vinyl benzyl)-3-Methylimidazole. villaumite;
(3) in proportion the polystyrene graft modification bead that 1g step (2) obtains is put into the phosphomolybdic acid of the 20mM of 50mL In aqueous solution, under the conditions of lucifuge, water-bath 30h at 25 DEG C, wash 30h under room temperature, vacuum lyophilization obtains polystyrene and urges Change bead.
Embodiment 2
A kind of polystyrene catalysis bead, makes by following method:
(1) polystyrene sphere is carried out pretreatment: successively with dehydrated alcohol, deionized water, 2% potassium hydroxide water-soluble Liquid, the aqueous sulfuric acid of 2% clean polystyrene sphere, are washed with deionized water to neutrality, vacuum lyophilization, obtain pretreatment Polystyrene sphere;
(2) preparation of polystyrene graft modification bead: pretreatment polystyrene sphere step (1) obtained, is dipped in 30min in the toluene solution of 5mM benzophenone, takes out and dries in atmosphere, is placed in hermetic container logical nitrogen 5min, then at ripple A length of 254nm, power are under the ultra-violet lamp of 4W, and irradiation distance is 5cm, irradiate 5min, take out, put into the ionic liquid of 0.1M Methanol solution in, nitrogen protection under, at 55 DEG C, react 48h;Successively with deionized water, washes of absolute alcohol, vacuum freezing Drying, ionic liquid forms poly ion liquid on polystyrene sphere surface, obtains polystyrene graft modification bead;Described step Suddenly the polystyrene sphere that (1) obtains is 1g:20mL with the ratio of the methanol solution of ionic liquid;
The ionic liquid of the present embodiment is: 1-(4-vinyl benzyl)-3-1-Butyl-1H-imidazole villaumite
(3) in proportion the polystyrene graft modification bead that 1g step (2) obtains is put into the phosphotungstic acid of the 25mM of 10mL In aqueous solution, under the conditions of lucifuge, water-bath 48h at 15 DEG C, wash 12h under room temperature, vacuum lyophilization obtains polystyrene and urges Change bead.
Embodiment 3
A kind of polystyrene catalysis bead, makes by following method:
(1) polystyrene sphere is carried out pretreatment: successively with dehydrated alcohol, deionized water, the sodium hydroxide water of 10% Solution, the aqueous hydrochloric acid solution of 10% clean polystyrene sphere, are washed with deionized water to neutrality, vacuum lyophilization, obtain pre- Process polystyrene sphere;
(2) preparation of polystyrene graft modification bead: pretreatment polystyrene sphere step (1) obtained, is dipped in 5min in the toluene solution of 25mM benzophenone, takes out and dries in atmosphere, is placed in hermetic container logical nitrogen 180min, then at Wavelength is 365nm, power be 12W ultra-violet lamp under, irradiation distance is 20cm, irradiate 30min, take out, put into 0.5M from In the methanol solution of sub-liquid, under nitrogen protection, at 65 DEG C, react 12h;Successively with deionized water, washes of absolute alcohol, very Air cooling freezes drying, and ionic liquid forms poly ion liquid on polystyrene sphere surface, obtains polystyrene graft modification bead; The polystyrene sphere that described step (1) obtains is 1g:30mL with the ratio of the methanol solution of ionic liquid;
The ionic liquid of the present embodiment is: 1-(4 vinyl benzyl)-3-Methylimidazole. bromide;
(3) in proportion the polystyrene graft modification bead that 1g step (2) obtains is put into the silicomolybdic acid of the 10mM of 100mL In aqueous solution, under the conditions of lucifuge, water-bath 12h at 35 DEG C, wash 48h under room temperature, vacuum lyophilization obtains polystyrene and urges Change bead.
Experiment proves: substitute 1-(4 vinyls of the present embodiment with 1-(4-vinyl benzyl)-3-1-Butyl-1H-imidazole smelling salts Benzyl)-3-Methylimidazole. bromide, other same the present embodiment, polystyrene catalysis bead can be prepared.
Experiment proves: the solvent of the benzophenone solution of embodiment 1-3 also can use heptane.
Slurry photocatalytic reactor is shown in Fig. 1, is 10L rectangular glass transmission container (10) including volume, at glass Be provided with aeration head (7) in light transmission container, the aeration pump (5) being arranged on outside glass transmission container by pipeline successively with gas stream Gauge (6) and aeration head (7) connect;The feed pipe one end being provided with the 1st valve (2) is connected with feed pump (1), and the other end is arranged In glass transmission container (10), it is outside equipped with two 55W daylight lamp (8) at glass transmission container (10), holds at glass transmission Flat polyvinylidene fluoride micro-filtration membrane original paper (9) and polystyrene catalysis bead (11), Kynoar it is additionally provided with in device (10) Flat micro-filtration original paper (9) by pipeline successively be arranged on glass transmission container (10) the 2nd valve (3) and discharging pump outward (4) connect.
Experiment:
In glass transmission container, it is passed through 6L waste water from dyestuff (dyestuff is Acid Orange II), prepares in pH=1, embodiment 1 When polystyrene catalysis concentration of small ball is 0.5g/L, Hydraulic retention time is 4h, aeration rate is 4L/min, degraded 0.2g/L acid Property orange II dyestuff, Acid Orange II degradation rate reaches 100% in 100min.
In glass transmission container, it is passed through 6L waste water from dyestuff (dyestuff is Acid Orange II), prepares in pH=1, embodiment 2 When polystyrene catalysis concentration of small ball is 0.5g/L, Hydraulic retention time is 4h, aeration rate is 4L/min, degraded 0.1g/L acid Property orange II dyestuff, Acid Orange II degradation rate reaches 94% in 100min.
In glass transmission container, it is passed through 6L waste water from dyestuff (dyestuff is Acid Orange II), prepares in pH=1, embodiment 3 When polystyrene catalysis concentration of small ball is 0.2g/L, Hydraulic retention time is 4h, aeration rate is 4L/min, degraded 0.2g/L acid Property orange II dyestuff Acid Orange II degradation rate reaches 84% in 100min.
It is demonstrated experimentally that the material of light transmission container can also select polymethyl methacrylate.
Acid Orange II selected by the dyestuff of the present invention, merely to enable those skilled in the art to be more fully understood that this Bright, other similar to Acid Orange II character stains thing all can be catalyzed bead with the polystyrene of the present invention and floated light be urged Change reactor and carry out degraded removal.

Claims (7)

1. a polystyrene catalysis bead, is characterized in that making by following method:
(1) polystyrene sphere is carried out pretreatment: successively with dehydrated alcohol, deionized water, the inorganic base aqueous solution of 2-10%, The inorganic acid aqueous solution of 2-10% cleans polystyrene sphere, is washed with deionized water to neutrality, vacuum lyophilization, obtains pre-place Reason polystyrene sphere;
(2) preparation of polystyrene graft modification bead: pretreatment polystyrene sphere step (1) obtained, is dipped in 5- 5-30min in the toluene solution of 25mM benzophenone or the n-heptane solution of 5-25mM benzophenone, takes out and dries in atmosphere, put Logical nitrogen 5-180min in hermetic container, then at wavelength be 254-365nm, power be 4-12W ultra-violet lamp under, irradiate away from From for 5-20cm, irradiate 5-30min, take out, in the methanol solution of the ionic liquid putting into 0.1-0.5M, under nitrogen protection, At 55-65 DEG C, react 12-48h;Successively with deionized water, washes of absolute alcohol, vacuum freezing is dried, is obtained polystyrene and connect The modified bead of branch;The polystyrene sphere that described step (1) obtains is 1g:20-30mL with the ratio of the methanol solution of ionic liquid;
(3) in proportion the polystyrene graft modification bead that 1g step (2) obtains is put into 10-25mM miscellaneous many of 10-100mL In aqueous acid, under the conditions of lucifuge, water-bath 12-48h at 15-35 DEG C, wash 12-48h under room temperature, vacuum lyophilization obtains Polystyrene catalysis bead.
The most according to claim 1, polystyrene catalysis bead, is characterized in that described inorganic base is sodium hydroxide or hydroxide Potassium.
The most according to claim 1, polystyrene catalysis bead, is characterized in that described mineral acid is hydrochloric acid or sulphuric acid.
The most according to claim 1, polystyrene catalysis bead, is characterized in that described ionic liquid is 1-(4-vinyl benzyl Base)-3-Methylimidazole. villaumite, 1-(4-vinyl benzyl)-3-1-Butyl-1H-imidazole villaumite, 1-(4 vinyl benzyl)-3-methyl miaow Azoles bromide or 1-(4-vinyl benzyl)-3-1-Butyl-1H-imidazole smelling salts.
The most according to claim 1 polystyrene catalysis bead, it is characterized in that described heteropoly acid is: phosphomolybdic acid, phosphotungstic acid or Silicomolybdic acid.
6. slurry photocatalytic reactor includes light transmission container (10), is provided with aeration head (7), is arranged in light transmission container Aeration pump (5) outside light container is connected with gas flowmeter (6) and aeration head (7) successively by pipeline;It is provided with the 1st valve (2) feed pipe one end is connected with feed pump (1), and the other end is arranged in light transmission container (10), at light transmission container (10) peripheral hardware It is equipped with daylight lamp (8), it is characterized in that in light transmission container (10), be additionally provided with flat polyvinylidene fluoride micro-filtration membrane original paper (9) and power Profit require one of 1-5 polystyrene catalysis bead (11), flat polyvinylidene fluoride micro-filtration membrane original paper (9) by pipeline successively with It is arranged on outer the 2nd valve (3) of light transmission container (10) and discharging pump (4) connects.
Slurry photocatalytic reactor the most according to claim 6, is characterized in that the material of described light transmission container is glass Or polymethyl methacrylate.
CN201610547242.1A 2016-07-12 2016-07-12 Polystyrene catalysis bead and slurry photocatalytic reactor Pending CN106179498A (en)

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Cited By (1)

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Application publication date: 20161207