CN107930347A - A kind of plant absorption liquid of phenyl ring class VOCs and preparation method thereof - Google Patents

A kind of plant absorption liquid of phenyl ring class VOCs and preparation method thereof Download PDF

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Publication number
CN107930347A
CN107930347A CN201711184719.5A CN201711184719A CN107930347A CN 107930347 A CN107930347 A CN 107930347A CN 201711184719 A CN201711184719 A CN 201711184719A CN 107930347 A CN107930347 A CN 107930347A
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parts
oil
plant
liquid
absorption liquid
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雷晓华
黄�俊
符家振
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Guangdong Guangdong Four Public Environmental Protection Service Co Ltd
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Guangdong Guangdong Four Public Environmental Protection Service Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1493Selection of liquid materials for use as absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1487Removing organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/50Combinations of absorbents
    • B01D2252/504Mixtures of two or more absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702Hydrocarbons
    • B01D2257/7027Aromatic hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Fats And Perfumes (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

The invention belongs to phenyl ring class VOCs to absorb processing technology field.It is difficult to the technical problem to form micella to solve, plant absorption liquid not high to phenyl ring class VOCs absorption efficiencies and phenyl ring class VOCs in the prior art, there is provided a kind of plant absorption liquid of phenyl ring class VOCs and preparation method thereof, the plant absorption liquid includes plant extraction liquid;The plant extraction liquid includes the component of following parts by weight:23 parts of 8 13 parts of peppermint oil, 68 parts of camphor oil, 79 parts of cinnamon oil, 68 parts of lemon oil, 36 parts of pine-tree oil, 34 parts of cedar oil, 23 parts of spearmint oil and eucalyptus oil.The preparation method includes step:A, plant extraction liquid is prepared:Plant extracts is crushed and is placed in extraction kettle, methanol is added and ethanol is extracted, obtain plant extraction liquid;B, plant absorption liquid is prepared:By plant extraction liquid and emulsion after mixing, plant absorption liquid is made.The present invention has the characteristics that absorptivity is high, cost is low.

Description

A kind of plant absorption liquid of phenyl ring class VOCs and preparation method thereof
Technical field
The invention belongs to phenyl ring class VOCs to absorb processing technology field, and in particular to a kind of plant absorption of phenyl ring class VOCs Liquid and preparation method thereof.
Background technology
Plant absorption liquid is a kind of VOCs administering methods of environment-friendly type.Plant absorption liquid is 30% usually with mass fraction Ethanol or methanol extract bark at 45 DEG C or water obtains, which has methyl mercaptan high removal rate (97.2%), C is used13- nuclear magnetic resonance (NMR) method analyzes the extracting solution, its main active is (-) table in polyphenol mixture Catechin (EC).By olive leaf, the waste water of olive oil product, carried with the ethanol water that mass fraction is 50% at 60 DEG C Take 4h to obtain extract, it is found that this extract has armpit lasting deodorizing effect.Being extracted from big tangerine persimmon has removal Machine rubbish stench, footwear are smelly, halitosis has efficient deodorant.
Polyphenols has relatively more activated groups, and reaction generation quinones substance is easily carried out with VOCs tail gas (to be had It is pink).In addition, the part organic exhaust gas after catalytic oxidation, part chain rupture generation low molecule organic matter, portion It is mitogenetic into soluble easily in water or organic liquor alcohols or acid, and absorbed by vegetation water.
However, its specific assimilation effect and absorption efficiency be not often good enough.If add the surface in the water of vegetation water Active material continues to increase, and reaches a certain limit (commonly referred to as critical micelle concentration, represented with CMC), then except being enriched in boundary It is unnecessary to form the hydrophilic group stretched in water and the micella lipophilic group being close together in water outside face.This micella is parent What oil base was close together, this allows for the benzene class steam that it is absorbed and is wrapped among micella, so as to generate " solubilising " work With.It is contemplated that with the increase of micella, " solubilising " effect also will increase.The least concentration for being usually formed critical micell about exists 0.01~0.4% (weight) left and right.But with aqueous solution surface reactive material be on the increase, will occur between micella Close emigrant, form the increasing micelle of volume, they are due to being hydrophilic group towards in water, it is impossible to make benzene class steam through micelle and Into wherein, therefore the concentration of unconfined enlarged surface active material will be nonsensical.That is, solubilization is that have Limit.For some nonpolar organic matters, the solubility such as the organic matter of benzene,toluene,xylene etc is minimum, and is difficult Form critical micell.In addition, the complicated component of vegetation water, layman is difficult to understand which component to containing phenyl ring class VOCs With effective absorption, and uptake is difficult to hold.
The content of the invention
It is an object of the invention to solve above technical problem existing in the prior art at least one of, there is provided a kind of benzene Plant absorption liquid of ring class VOCs and preparation method thereof.
The purpose of the present invention is what is be achieved through the following technical solutions:
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:8-13 parts of peppermint oil, 6-8 parts of camphor oil, 7-9 parts of cinnamon oil, 6-8 parts of lemon oil, 3-6 parts of pine-tree oil, cedar oil 2-3 parts of 3-4 parts, 2-3 parts of spearmint oil and eucalyptus oil.
Further, the plant extraction liquid includes the component of following parts by weight:9 parts of peppermint oil, 6.5 parts of camphor oil, meat 2.2 parts of 7.5 parts of oil of bay, 6.5 parts of lemon oil, 4 parts of pine-tree oil, 3.5 parts of cedar oil, 2.2 parts of spearmint oil and eucalyptus oil.
Further, emulsion is further included;The percetage by weight of plant extraction liquid and emulsion in the plant absorption liquid Respectively 15% and 85%.
Further, the emulsion includes the component of following parts by weight:35 parts of water, 25 parts of ethanol, 20 parts of methanol, table 2 parts~3 parts of face activating agent, 2 parts of inorganic salts.
Further, the surfactant is nonionic surface active agent Tween 20 or TX-10.
A kind of preparation method of the plant absorption liquid of phenyl ring class VOCs, including step:
A, plant extraction liquid is prepared:Plant extracts is crushed and is placed in extraction kettle, methanol is added and ethanol is extracted, Obtain plant extraction liquid;
B, plant absorption liquid is prepared:By plant extraction liquid and emulsion after mixing, plant absorption liquid is made.
Further, the plant extracts in step A described in the plant extracts in the step A by following plants leaf Son composition:Peppermint, camphor tree, xylocinnamomum, lemon, orange tree, deodar, spearmint and eucalyptus.
Further, the extraction conditions of the extraction kettle in the step A is:Extracting pressure 8-10MPa, extraction temperature 45 DEG C, carbon dioxide flow 22-28L/h;Extraction time is 1.5-5.5h.
It is of the invention to be relative to the beneficial effect of the prior art:The plant absorption liquid and its system of the phenyl ring class VOCs of the present invention Preparation Method has following beneficial effect:(1) each non-volatile or volatility very little contained in plant extraction liquid of the invention And effect of dissolving each other well can be produced with benzene, toluene and dimethylbenzene with the immiscible heterocyclic arene class material of water, while it contains Some hydrophilic radicals can mix with aqueous solution well again, so as to play the effect of solubilising, after it forms emulsion liquid, can show Write the absorption treatment effeciency improved to phenyl ring class VOCs.(2) plant extraction liquid of the invention can reduce reconstituted emulsion distillation amount 50-70%, greatly reduces operating cost, this method is easy to operate, suitable for practical application.
Embodiment
Technical scheme is described in detail with reference to embodiments, it should be noted that be only below The preferred embodiment of the present invention, for those of ordinary skill in the art, before the invention design is not departed from Put, various modifications and improvements can be made, these should belong to protection scope of the present invention.
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:8-13 parts of peppermint oil, 6-8 parts of camphor oil, 7-9 parts of cinnamon oil, 6-8 parts of lemon oil, 3-6 parts of pine-tree oil, cedar oil 2-3 parts of 3-4 parts, 2-3 parts of spearmint oil and eucalyptus oil.
Since the solubility of benzene,toluene,xylene in water is minimum, therefore, it is necessary to some active components are added in water, Make the solubility increase of benzene vapour in aqueous, produce so-called solubilization, then using foam separating technology, select suitable When equipment achieve the purpose that purification containing exhaust gas such as benzene spray painting, baking finish.The organic steams such as benzene,toluene,xylene in water molten Xie Du is minimum.This is because benzene, toluene etc. belong to apolar substance, they will produce row mutually between the hydrone of polarity Reprimand acts on and is difficult to be dissolved in water.In order to increase the solubility of benzene vapour in water, it is existing hydrophilic that certain can be added in water Base (it easy to combined with water) and there is the plant extraction liquid component of lipophilic group (it is easy to and benzene molecular combination).
In the plant extraction liquid of the present invention, peppermint oil, camphor oil, cinnamon oil, lemon oil, pine-tree oil, cedar oil, spearmint oil It is non-volatile or volatility very little and the immiscible heterocyclic arene class material of water with the material such as eucalyptus oil, to benzene, toluene and diformazan The organic gas such as benzene play dissolution, after adding surfactant, form emulsion liquid, so as to play solubilization, carry The high absorption treatment effeciency to phenyl ring class VOCs.
Further, the plant extraction liquid includes the component of following parts by weight:9 parts of peppermint oil, 6.5 parts of camphor oil, meat 2.2 parts of 7.5 parts of oil of bay, 6.5 parts of lemon oil, 4 parts of pine-tree oil, 3.5 parts of cedar oil, 2.2 parts of spearmint oil and eucalyptus oil.
Further, emulsion is further included;The percetage by weight of plant extraction liquid and emulsion in the plant absorption liquid Respectively 15% and 85%.
Further, the emulsion includes the component of following parts by weight:35 parts of water, 25 parts of ethanol, 20 parts of methanol, table 2 parts~3 parts of face activating agent, 2 parts of inorganic salts.
Further, the surfactant is nonionic surface active agent Tween 20 or TX-10.
A kind of preparation method of the plant absorption liquid of phenyl ring class VOCs, including step:
A, plant extraction liquid is prepared:Plant extracts is crushed and is placed in extraction kettle, methanol is added and ethanol is extracted, Obtain plant extraction liquid;
B, plant absorption liquid is prepared:By plant extraction liquid and emulsion after mixing, plant absorption liquid is made.
Further, the plant extracts in the step A is the plant extracts in the step A by following plants Leaf forms:Peppermint, camphor tree, xylocinnamomum, lemon, orange tree, deodar, spearmint and eucalyptus.
Further, the extraction conditions of the extraction kettle in the step A is:Extracting pressure 8-10MPa, extraction temperature 45 DEG C, carbon dioxide flow 22-28L/h;Extraction time is 1.5-5.5h.
Specifically, method is as follows:
Plant extracts is subjected to brokenly essence into powder, extraction kettle is placed in, adds a certain amount of methanol, ethanol extract, extract Pressure power 8-10Mpa, 45 DEG C of extraction temperature, CO2Flow 22-28L/h, is 1.5- in the extraction time of Accelerate solvent extraction instrument 5.5h, removes solid slag, collects vegetation water (without dehydration), retains the active ingredient of natural plant liquid, obtain following weight The component of part:8-13 parts of peppermint oil, 6-8 parts of camphor oil, 7-9 parts of cinnamon oil, 6-8 parts of lemon oil, 3-6 parts of pine-tree oil, cedar oil 3-4 Part, 2-3 parts of spearmint oil, 2-3 parts of eucalyptus oil.
Accelerate solvent extraction instrument characteristic:In the active ingredient of Accelerate solvent extraction instrument extraction natural plant liquid by titanium dioxide The protective effect of carbon, extraction temperature are 45 DEG C, extraction time 1.5-5.5h, remove solid slag, and plant is collected without dehydration Liquid, saves solvent, and the active ingredient polyphenols for retaining natural plant liquid is not destroyed.
Technical parameter:Nonionic surface active agent is more likely formed microemulsion after being combined with cosurfactant, and micro- Lotion improves the solubilizing amount and solubilising power of indissoluble thing therewith.Such as sodium laurate, it has CH3·CH2……CH2·CH2- Paraffin wax base (lipophilic group), meanwhile, it has-COONa hydrophilic groups again.This formula adds the nonionic surface active agent of 2-3% Tween 20 or TX-10 (alkylphenol polyoxyethylene ether), adds the too high easily generation bubble of concentration of surfactant.
1. plant absorption liquid component and its component act on accordingly
Each component material in plant absorption liquid is non-volatile or volatility very little and the immiscible heterocyclic arene class thing of water Matter, dissolution is played to organic gas such as benzene, toluene and dimethylbenzene.After adding surfactant, emulsion liquid, its effect are formed It is more notable.Each component effect of specific plant absorption liquid see the table below 1.
1 plant absorption liquid component of table and its component act on distribution table accordingly
2. plant absorption liquid absorbs phenyl ring class VOCs efficiency tests
Nonionic surface active agent is more likely formed microemulsion after being combined with cosurfactant, and microemulsion is to indissoluble The solubilizing amount and solubilising power of thing improve therewith.Absorbing especially toluene using microemulsion solubilising has good effect.With Exemplified by Tween 20- n-butylamine-toluene-water microemulsion systems, the mass fraction of toluene can reach 80.80%, i.e., per 100g Ion in Nonionic Microemulsion can absorb 421g toluene with increase-volume, but the solubility of toluene in water is extremely low.In addition for TX 405- N-butylamine-toluene-water microemulsion system, the mass fraction of toluene can reach 82.72%, i.e., per 100g Ion in Nonionic Microemulsion 478.7g toluene can be absorbed with increase-volume.
Embodiment 1
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:8 parts of peppermint oil, 6 parts of camphor oil, 7 parts of cinnamon oil, 6 parts of lemon oil, 3 parts of pine-tree oil, 3 parts of cedar oil, spearmint oil 2 parts and 2 parts of eucalyptus oil.
Embodiment 2
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:13 parts of peppermint oil, 8 parts of camphor oil, 9 parts of cinnamon oil, 8 parts of lemon oil, 6 parts of pine-tree oil, 4 parts of cedar oil, spearmint 3 parts of 3 parts of oil and eucalyptus oil.
Plant absorption liquid further includes emulsion;The percetage by weight of plant extraction liquid and emulsion is distinguished in plant absorption liquid For 15% and 85%.Emulsion includes the component of following parts by weight:35 parts of water, 25 parts of ethanol, 20 parts of methanol, Tween 20 are non- 2 parts of ionic surfactant, 2 parts of inorganic salts.
Embodiment 3
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:10 parts of peppermint oil, 7 parts of camphor oil, 8 parts of cinnamon oil, 7 parts of lemon oil, 5 parts of pine-tree oil, 3.5 parts of cedar oil, stay orchid 2.5 parts of 2.5 parts of sesame oil and eucalyptus oil;Plant absorption liquid further includes emulsion;Plant extraction liquid and breast in the plant absorption liquid The percetage by weight for changing liquid is respectively 15% and 85%.The emulsion includes the component of following parts by weight:35 parts of water, ethanol 25 parts, 20 parts of methanol, 3 parts of TX-10 nonionic surface active agent, 2 parts of inorganic salts.
Embodiment 4
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:9 parts of peppermint oil, 6.5 parts of camphor oil, 7.5 parts of cinnamon oil, 6.5 parts of lemon oil, 4 parts of pine-tree oil, 3.5 parts of cedar oil, 2.2 parts of 2.2 parts of spearmint oil and eucalyptus oil;The plant absorption liquid further includes emulsion;Plant carries in the plant absorption liquid It is respectively 15% and 85% to take the percetage by weight of liquid and emulsion;The emulsion includes the component of following parts by weight:Water 35 parts, 25 parts of ethanol, 20 parts of methanol, 2.5 parts of surfactant, 2 parts of inorganic salts.
Embodiment 5
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:13 parts of peppermint oil, 8 parts of camphor oil, 9 parts of cinnamon oil, 8 parts of lemon oil, 6 parts of pine-tree oil, 4 parts of cedar oil, spearmint 3 parts of 3 parts of oil and eucalyptus oil;Plant absorption liquid further includes emulsion;The weight of plant extraction liquid and emulsion in plant absorption liquid Percentage is respectively 15% and 85%.Emulsion includes the component of following parts by weight:35 parts of water, 25 parts of ethanol, 20 parts of methanol, 2 parts of 20 nonionic surface active agent of Tween, 2 parts of inorganic salts.
The preparation method of the plant absorption liquid of phenyl ring class VOCs, including step:A, plant extraction liquid is prepared:By plant extract Thing is crushed and is placed in extraction kettle, adds methanol and ethanol is extracted, obtain plant extraction liquid;B, plant absorption liquid is prepared:Will With emulsion after mixing, plant absorption liquid is made in plant extraction liquid.Plant extracts in the step A is by following plants Leaf composition:Peppermint, camphor tree, xylocinnamomum, lemon, orange tree, deodar, spearmint and eucalyptus.Extraction kettle in the step A Extraction conditions be:Extracting pressure 8MPa, 45 DEG C of extraction temperature, carbon dioxide flow 22L/h;Extraction time is 1.5h.
Embodiment 6
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:10 parts of peppermint oil, 7 parts of camphor oil, 8 parts of cinnamon oil, 7 parts of lemon oil, 5 parts of pine-tree oil, 3.5 parts of cedar oil, stay orchid 2.5 parts of 2.5 parts of sesame oil and eucalyptus oil;Plant absorption liquid further includes emulsion;Plant extraction liquid and breast in the plant absorption liquid The percetage by weight for changing liquid is respectively 15% and 85%.The emulsion includes the component of following parts by weight:35 parts of water, ethanol 25 parts, 20 parts of methanol, 3 parts of TX-10 nonionic surface active agent, 2 parts of inorganic salts.
The preparation method of the plant absorption liquid of phenyl ring class VOCs, including step:
A, plant extraction liquid is prepared:Plant extracts is crushed and is placed in extraction kettle, methanol is added and ethanol is extracted, Obtain plant extraction liquid;B, plant absorption liquid is prepared:By plant extraction liquid and emulsion after mixing, plant absorption is made Liquid.Plant extracts in the step A is made of the leaf of following plants:Peppermint, camphor tree, xylocinnamomum, lemon, orange tree, Deodar, spearmint and eucalyptus.
The extraction conditions of extraction kettle in the step A is:Extracting pressure 10MPa, 45 DEG C of extraction temperature, carbon dioxide stream Measure as 28L/h;Extraction time is 5.5h.
Embodiment 7
A kind of plant absorption liquid of phenyl ring class VOCs, including plant extraction liquid;The plant extraction liquid includes following weight The component of number:9 parts of peppermint oil, 6.5 parts of camphor oil, 7.5 parts of cinnamon oil, 6.5 parts of lemon oil, 4 parts of pine-tree oil, 3.5 parts of cedar oil, 2.2 parts of 2.2 parts of spearmint oil and eucalyptus oil;The plant absorption liquid further includes emulsion;Plant carries in the plant absorption liquid It is respectively 15% and 85% to take the percetage by weight of liquid and emulsion;The emulsion includes the component of following parts by weight:Water 35 parts, 25 parts of ethanol, 20 parts of methanol, 2.5 parts of 20 nonionic surface active agent of Tween, 2 parts of inorganic salts.
The preparation method of the plant absorption liquid of phenyl ring class VOCs, including step:
A, plant extraction liquid is prepared:Plant extracts is crushed and is placed in extraction kettle, methanol is added and ethanol is extracted, Obtain plant extraction liquid;B, plant absorption liquid is prepared:By plant extraction liquid and emulsion after mixing, plant absorption is made Liquid.Plant extracts in the step A is made of the leaf of following plants:Peppermint, camphor tree, xylocinnamomum, lemon, orange tree, Deodar, spearmint and eucalyptus.
The extraction conditions of extraction kettle in the step A is:Extracting pressure 9MPa, 45 DEG C of extraction temperature, carbon dioxide stream Measure as 26L/h;Extraction time is 3.5h.
Test case
The organic exhaust gas composition of certain factory is simulated, is mixed after benzene,toluene,xylene liquid is vaporized by a certain percentage with air Close and be sent into absorption tower, air inlet composition is 1500mg/m containing benzene3(1.5ppm), toluene 500mg/m3(0.5ppm), dimethylbenzene 1000mg/m3(1ppm).The prepared emulsion in embodiment 5,6 or 7 is pumped up to tower top spraying into, with gaseous mixture adverse current phase Meet, the organic component in mixed gas is absorbed into liquid phase.It is equipped with system into and out of tower gas sample mouth, sampling.Gas is through gas The absorptivity of each emulsion is calculated after the analysis of analysis of hplc instrument.Experimental data is as shown in table 2.
2 absorption experiment tables of data of table
Following conclusion can be drawn according to above test case:
1) it is feasible with the scheme of the benzene in emulsion absorption process processing organic exhaust gas, toluene and dimethylbenzene.The program The key of implementation is the preparation of emulsion.
2) the demulsification regeneration of emulsion is the characteristics of this method protrudes.It is demulsified after emulsion saturation through acid adding, with sedimentation After method initial gross separation, reconstituted emulsion distillation amount 50-70% can be reduced, greatly reduces operating cost, this method is easy to operate, Suitable for practical application.
3) rotating stream tray scrubber is a kind of higher novel absorbent tower of efficiency.In gas velocity it is 16.2m/s in this experiment, gas liquid ratio (V/L) under conditions of being 1095, the absorptivity of rotating stream tray scrubber used in experiment is up to 70%.
The record of specification can preferably realize technical scheme according to the present invention.

Claims (8)

1. a kind of plant absorption liquid of phenyl ring class VOCs, it is characterised in that including plant extraction liquid;The plant extraction liquid includes The component of following parts by weight:8-13 parts of peppermint oil, 6-8 parts of camphor oil, 7-9 parts of cinnamon oil, 6-8 parts of lemon oil, pine-tree oil 3-6 Part, 3-4 parts of cedar oil, 2-3 parts of spearmint oil and 2-3 parts of eucalyptus oil.
A kind of 2. plant absorption liquid of phenyl ring class VOCs according to claim 1, it is characterised in that the plant extraction liquid Include the component of following parts by weight:9 parts of peppermint oil, 6.5 parts of camphor oil, 7.5 parts of cinnamon oil, 6.5 parts of lemon oil, 4 parts of pine-tree oil, 2.2 parts of 3.5 parts of cedar oil, 2.2 parts of spearmint oil and eucalyptus oil.
3. the plant absorption liquid of a kind of phenyl ring class VOCs according to claim 1 or 2, it is characterised in that further include emulsification Liquid;The percetage by weight of plant extraction liquid and emulsion is respectively 15% and 85% in the plant absorption liquid.
4. the plant absorption liquid of a kind of phenyl ring class VOCs according to claim 3, it is characterised in that the emulsion includes The component of following parts by weight:35 parts of water, 25 parts of ethanol, 20 parts of methanol, 2 parts~3 parts of surfactant, 2 parts of inorganic salts.
A kind of 5. plant absorption liquid of phenyl ring class VOCs according to claim 4, it is characterised in that the surfactant For nonionic surface active agent Tween 20 or TX-10.
A kind of a kind of 6. preparation method of the plant absorption liquid of phenyl ring class VOCs described in claim 4 or 5, it is characterised in that Including step:
A, plant extraction liquid is prepared:Plant extracts is crushed and is placed in extraction kettle, methanol is added and ethanol is extracted, obtain Plant extraction liquid;
B, plant absorption liquid is prepared:By plant extraction liquid and emulsion after mixing, plant absorption liquid is made.
7. the preparation method of the plant absorption liquid of a kind of phenyl ring class VOCs according to claim 6, it is characterised in that described Plant extracts in step A is made of the leaf of following plants:Peppermint, camphor tree, xylocinnamomum, lemon, orange tree, deodar, stay Lan Xiang and eucalyptus.
8. the preparation method of the plant absorption liquid of a kind of phenyl ring class VOCs according to claim 7, it is characterised in that described The extraction conditions of extraction kettle in step A is:Extracting pressure 8-10MPa, 45 DEG C of extraction temperature, carbon dioxide flow 22- 28L/h;Extraction time is 1.5-5.5h.
CN201711184719.5A 2017-11-23 2017-11-23 A kind of plant absorption liquid of phenyl ring class VOCs and preparation method thereof Pending CN107930347A (en)

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Publication number Priority date Publication date Assignee Title
CN109126447A (en) * 2018-09-19 2019-01-04 浙江瀚邦环保科技有限公司 A kind of lyosoption and its application method handling low-concentration organic exhaust gas
CN112295362A (en) * 2020-08-05 2021-02-02 汪昔奇 Purifying agent for removing formaldehyde, benzene, toluene, xylene, ammonia, TVOC and radon

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CN103463935A (en) * 2013-09-04 2013-12-25 南京大学 Absorbing emulsion of volatile organic compounds (VOCs) and preparation method of absorbing emulsion
CN104874276A (en) * 2015-06-04 2015-09-02 俞家琛 Plant solution deodorization device and method
CN105233318A (en) * 2015-10-13 2016-01-13 普罗生物技术(上海)有限公司 VOC (volatile organic compounds) dissolution promoter

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CN101947327A (en) * 2010-08-30 2011-01-19 江门市和馨香精技术有限公司 Deodorant
CN103463935A (en) * 2013-09-04 2013-12-25 南京大学 Absorbing emulsion of volatile organic compounds (VOCs) and preparation method of absorbing emulsion
CN104874276A (en) * 2015-06-04 2015-09-02 俞家琛 Plant solution deodorization device and method
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109126447A (en) * 2018-09-19 2019-01-04 浙江瀚邦环保科技有限公司 A kind of lyosoption and its application method handling low-concentration organic exhaust gas
CN112295362A (en) * 2020-08-05 2021-02-02 汪昔奇 Purifying agent for removing formaldehyde, benzene, toluene, xylene, ammonia, TVOC and radon

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