CN110721567A - Be applicable to lavatory developments dry process deodorization equipment - Google Patents
Be applicable to lavatory developments dry process deodorization equipment Download PDFInfo
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- CN110721567A CN110721567A CN201910956903.XA CN201910956903A CN110721567A CN 110721567 A CN110721567 A CN 110721567A CN 201910956903 A CN201910956903 A CN 201910956903A CN 110721567 A CN110721567 A CN 110721567A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/58—Ammonia
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/81—Solid phase processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
- B01D53/8606—Removing sulfur compounds only one sulfur compound other than sulfur oxides or hydrogen sulfide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
- B01D53/8612—Hydrogen sulfide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
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- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03D—WATER-CLOSETS OR URINALS WITH FLUSHING DEVICES; FLUSHING VALVES THEREFOR
- E03D9/00—Sanitary or other accessories for lavatories ; Devices for cleaning or disinfecting the toilet room or the toilet bowl; Devices for eliminating smells
- E03D9/04—Special arrangement or operation of ventilating devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/106—Peroxides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/608—Sulfates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/61—Phosphates
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Biomedical Technology (AREA)
- Public Health (AREA)
- Epidemiology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a device suitable for toilet dynamic dry deodorization, which comprises a fixed pipeline, a flow equalizer arranged in the fixed pipeline, an F6 grade plate filter, an oxidation bed A and an oxidation bed B. When the substrate plate is inactivated, the substrate plate can be prepared by the A oxidant or the B composite reactant again, so that the substrate plate can be repeatedly used, and the operation cost is reduced.
Description
Technical Field
The invention relates to the technical field of toilet odor treatment, in particular to a dynamic dry-method deodorization device suitable for a toilet.
Background
The toilet is a living behavior of people, and if the toilet is not managed, urine stains and excrement in the toilet are easy to decay and volatilize. After a long time, certain peculiar smell can be generated, the ambient air can be influenced, meanwhile, a large amount of bacteria such as mosquitoes, flies and the like can be bred, and the harm is brought to the health of people in the toilet. The only way to solve the odor of the toilet is that only the manager can clean the toilet in time, and simultaneously, the manager can start ventilation to exchange the indoor air and the outdoor air of the toilet, so that the fresh air is led into the room, and the odor gas is led out of the room. The discharged odor gas in the toilet can not be directly discharged and also needs to be treated to be discharged, so the odor removing device for the toilet is designed.
Disclosure of Invention
The invention aims to provide a dynamic dry deodorizing device suitable for toilets, so as to solve the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme: the device comprises a fixed pipeline, a flow equalizer, an F6-grade plate filter, an oxidation bed A and an oxidation bed B, wherein the flow equalizer, the F6-grade plate filter, the oxidation bed A and the oxidation bed B are arranged in the fixed pipeline, odor gas enters through the air inlet end of the fixed pipeline and is sequentially contacted with the flow equalizer, the F6-grade plate filter, the oxidation bed A and the oxidation bed B, the oxidation bed A is formed by loading an oxidizing agent A on the surface of a base plate of silicon carbide, the oxidation bed B is formed by loading a composite reactant B on the surface of the base plate of the silicon carbide, the oxidizing agent A is composed of 30 mass percent of sodium sulfate Na2S2O8 and 1 mass percent of catalyst iron oxide FeO, and the composite reactant B is composed of 25 mass percent of sodium dihydrogen phosphate NaH2PO4 and 25 mass percent of MgSO 4.
Preferably, the oxidation bed A is prepared by the following specific steps:
s1, weighing 30% of Na2S2O8 and 1% of FeO according to the mass percentage, injecting the mixture into 70% of tap water, and stirring the mixture in the water by a stirrer until the medicaments are completely dissolved and mixed to obtain an oxidant A;
s2, soaking the silicon carbide substrate board in the oxidizing agent A, fishing out after soaking for a period of time, and air-drying to obtain the oxidation bed A.
Preferably, the oxidation bed B is prepared by the following specific steps:
s1, weighing 25% of NaH2PO4 and 25% of MgSO4 according to mass percentage, injecting into 50% tap water, and stirring in the water by a stirrer until the reagents are completely dissolved and mixed to obtain the B composite reactant;
s2, placing the silicon carbide substrate plate in the B composite reactant for soaking, fishing out after soaking for a period of time, and air-drying to obtain the oxidation bed B.
Preferably, the soaking time in step S2 is 15-20min per batch, and the air drying time is 200-300 min.
Preferably, the substrate plate of silicon carbide is a foamed silicon carbide ceramic plate.
Preferably, the deodorizing method of the malodor removing apparatus comprises the steps of:
s1, enabling the odor gas to enter through the air inlet end of the fixed pipeline, firstly, carrying out flow equalization and distribution on the odor gas through a flow equalizer, and simultaneously carrying out primary filtration;
s2, enabling the gas to enter an F6-level plate filter after passing through a flow equalizer, and further filtering the gas;
s3, making the gas pass through a F6-level plate filter and then enter an oxidation bed A for oxidation reaction;
and S4, the gas passes through the oxidation bed A and then enters the oxidation bed B for composite reaction.
Compared with the prior art, the invention has the beneficial effects that:
after the reaction with the oxidation bed A and the oxidation bed B, except the flow rate of gas in a fixed pipeline, the treatment process can be completed without any other auxiliary conditions, so that the treatment effect is achieved, and the oxidation bed A and the oxidation bed B can be conveniently combined, carried and transported. When the substrate plate is inactivated, the substrate plate can be prepared by the A oxidant or the B composite reactant again, so that the substrate plate can be repeatedly used, and the operation cost is reduced.
Drawings
Fig. 1 is a schematic structural view of the whole of the present invention.
In the figure: 1. a current equalizer; 2. grade F6 plate filter; 3. an oxidation bed A; 4. an oxidation bed B; 5. and (5) fixing the pipeline.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "vertical", "upper", "lower", "horizontal", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of describing the present invention and simplifying the description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention.
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood by those skilled in the art according to specific situations.
Referring to fig. 1, the present invention provides a technical solution: the utility model provides a be applicable to lavatory developments dry method deodorization equipment, includes fixed pipeline 5 and installs the equalizer 1, F6 level plate filter 2, oxidation bed A3 and oxidation bed B4 inside fixed pipeline 5, and peculiar smell gas gets into through the inlet end of fixed pipeline 5 and contacts with equalizer 1, F6 level plate filter 2, oxidation bed A3 and oxidation bed B4 in proper order, oxidation bed A3 is formed by the loading of A oxidant in the substrate plate surface of carborundum, oxidation bed B4 is formed by the loading of B composite reactant in the substrate plate surface of carborundum, A oxidant is by the mass percent of 30% sodium sulfate Na2S2O8 and the mass percent is 1 thousandth catalyst iron oxide FeO, B composite reactant is by the mass percent of 25% sodium dihydrogen phosphate NaH2PO4 and the mass percent of 25% magnesium sulfate 4.
Further, the specific preparation steps of the oxidation bed A3 are as follows:
s1, weighing 30% of Na2S2O8 and 1% of FeO according to the mass percentage, injecting the mixture into 70% of tap water, and stirring the mixture in the water by a stirrer until the medicaments are completely dissolved and mixed to obtain an oxidant A;
s2, soaking the silicon carbide substrate plate in the oxidizing agent A, fishing out after soaking for a period of time, and air-drying to obtain the oxidation bed A3.
Further, the oxidation bed B4 is prepared by the following steps:
s1, weighing 25% of NaH2PO4 and 25% of MgSO4 according to mass percentage, injecting into 50% tap water, and stirring in the water by a stirrer until the reagents are completely dissolved and mixed to obtain the B composite reactant;
s2, placing the silicon carbide substrate plate in the B composite reactant for soaking, fishing out after soaking for a period of time, and air-drying to obtain the oxidation bed B4.
Further, the soaking time in step S2 is 15-20min per batch, and the air drying time is 200-300 min.
Further, the substrate plate of the silicon carbide is a foam silicon carbide ceramic plate.
Further, the deodorizing method of the malodor eliminating apparatus includes the steps of:
s1, allowing the odor gas to enter through the air inlet end of the fixed pipeline 5, firstly, carrying out flow equalization and distribution on the odor gas through the flow equalizer 1, and simultaneously carrying out primary filtration;
s2, enabling the gas to enter an F6-level plate type filter 2 after passing through a flow equalizer 1, and further filtering the gas;
s3, the gas enters an oxidation bed A3 to carry out oxidation reaction after passing through a F6-level plate filter 2;
s4, the gas passes through the oxidation bed A3 and then enters the oxidation bed B4 to carry out composite reaction.
The working principle is as follows: when the malodorous pollutant factors in the odorous gas diffuse to the active centers on the surface of the oxidation bed A3 or the oxidation bed B4 in a dynamic form, the malodorous pollutant factors chemically react with the oxidized molecules on the oxidation bed A3 or the oxidation bed B4. According to the transient reaction mechanism, the malodor contaminating factors are decomposed into small molecular compounds and odorless molecules. So that the deodorizing effect can be achieved,
the peculiar smell gas of the toilet mainly comprises:
hydrogen sulfide H2S, having an egg odor;
ammonia NH3, a strongly irritating gas;
methanol CH3SH, having rotten cabbage smell;
fecal odor C9H9N, with putrefactive odor of feces liquid and feces;
the specific reaction mechanism is as follows:
hydrogen sulfide:
ammonia
Methyl mercaptan:
skatole:
to explain further: sulfate radicals (SO4) are radicals with higher redox potentials and are therefore believed to oxidize most organics under ideal conditions, as detailed in the above reaction mechanism.
The surface of the silicon carbide ceramic substrate plate is of a micropore accumulation structure, and the specific surface area is very large. When the substrate plate carries an oxidizing agent to perform oxidation reaction, the surface of the substrate plate is basically free of residues. When the struvite is loaded with sodium dihydrogen phosphate and magnesium sulfate, the struvite is sensitive to humidity in the air and is collected on the surface of the substrate after a long time to form struvite;
sulfate radicals attack N bonds and H bonds and directly destroy skatole structures to form heterocyclic substances and organic weak acids;
after the reaction with the oxidation bed A3 and the oxidation bed B4, the treatment process can be completed without any auxiliary conditions except for the need of fixing the flow rate of gas in the pipeline 5, so that the treatment effect is achieved, and the oxidation bed A3 and the oxidation bed B4 can be conveniently combined, carried and transported. When the substrate plate is inactivated, the substrate plate can be prepared by the A oxidant or the B composite reactant again, so that the substrate plate can be repeatedly used, and the operation cost is reduced.
The F6 grade plate filter and flow equalizer are well known in the art and their structure is not specifically disclosed herein.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a be applicable to lavatory developments dry process deodorization equipment which characterized in that: comprises a fixed pipeline (5), a flow equalizer (1), an F6 grade plate type filter (2), an oxidation bed A (3) and an oxidation bed B (4) which are arranged in the fixed pipeline (5), wherein peculiar smell gas enters through the air inlet end of the fixed pipeline (5) and is sequentially contacted with the flow equalizer (1), the F6 grade plate type filter (2), the oxidation bed A (3) and the oxidation bed B (4), the oxidation bed A (3) is formed by loading an oxidizing agent A on the surface of a base plate of silicon carbide, the oxidation bed B (4) is formed by loading the B composite reactant on the surface of a substrate plate of silicon carbide, the oxidant A consists of 30 percent by mass of oxidant sodium sulfate Na2S2O8 and 1 per mill of catalyst iron oxide FeO, the B composite reactant is composed of 25% sodium dihydrogen phosphate NaH2PO4 and 25% magnesium sulfate MgSO4 by mass.
2. The dynamic dry deodorizing equipment for toilets according to claim 1, wherein: the oxidation bed A (3) comprises the following specific preparation steps:
s1, weighing 30% of Na2S2O8 and 1% of FeO according to the mass percentage, injecting the mixture into 70% of tap water, and stirring the mixture in the water by a stirrer until the medicaments are completely dissolved and mixed to obtain an oxidant A;
s2, soaking the silicon carbide substrate board in the oxidizing agent A, fishing out after soaking for a period of time, and air-drying to obtain the oxidation bed A (3).
3. The dynamic dry deodorizing equipment for toilets according to claim 1, wherein: the oxidation bed B (4) is prepared by the following specific steps:
s1, weighing 25% of NaH2PO4 and 25% of MgSO4 according to mass percentage, injecting into 50% tap water, and stirring in the water by a stirrer until the reagents are completely dissolved and mixed to obtain the B composite reactant;
s2, placing the silicon carbide substrate plate in the B composite reactant for soaking, fishing out after soaking for a period of time, and air-drying to obtain the oxidation bed B (4).
4. The dynamic dry deodorizing equipment for toilets according to claim 5, wherein said equipment comprises: in step S2, the soaking time is 15-20min per batch, and the air drying time is 200-300 min.
5. The dynamic dry deodorizing equipment for toilets according to claim 1, wherein: the substrate plate of the silicon carbide is a foam silicon carbide ceramic plate.
6. The dynamic dry deodorizing equipment for toilets according to claim 1, wherein: the deodorizing method of the deodorizing equipment comprises the following steps:
s1, enabling the odor gas to enter through the air inlet end of the fixed pipeline (5), firstly, carrying out flow equalization and distribution on the odor gas through the flow equalizer (1), and simultaneously carrying out primary filtration;
s2, enabling the gas to enter an F6-level plate filter (2) after passing through a flow equalizer (1), and further filtering the gas;
s3, allowing the gas to pass through an F6-level plate filter (2) and then enter an oxidation bed A (3) for oxidation reaction;
s4, the gas passes through the oxidation bed A (3) and then enters the oxidation bed B (4) for composite reaction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910956903.XA CN110721567A (en) | 2019-10-10 | 2019-10-10 | Be applicable to lavatory developments dry process deodorization equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910956903.XA CN110721567A (en) | 2019-10-10 | 2019-10-10 | Be applicable to lavatory developments dry process deodorization equipment |
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| CN110721567A true CN110721567A (en) | 2020-01-24 |
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| CN201910956903.XA Pending CN110721567A (en) | 2019-10-10 | 2019-10-10 | Be applicable to lavatory developments dry process deodorization equipment |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4343765A (en) * | 1980-12-11 | 1982-08-10 | Georgia Tech Research Institute | Method for deodorizing and disinfecting air |
| CN1833730A (en) * | 2006-04-21 | 2006-09-20 | 王锡麟 | Public lavatory deodorant and prepn. thereof |
| CN204637987U (en) * | 2015-04-21 | 2015-09-16 | 南京朗洁环保科技有限公司 | A kind of hydrogen sulfide removal system based on photocatalysis spray |
| CN205461711U (en) * | 2016-01-29 | 2016-08-17 | 上海鸿来环保设备有限公司 | Static, photodissociation, compound all -in -one of catalysis |
| CN107020003A (en) * | 2016-01-29 | 2017-08-08 | 上海鸿来环保设备有限公司 | The Odor absorbers of lipid waste gas, peculiar smell baffle, the preparation method of the peculiar smell baffle, dry method technology of deodorization and its equipment |
| CN107115780A (en) * | 2017-04-25 | 2017-09-01 | 重庆安欣环保节能科技有限公司 | A kind of medicament and its deodorizing method for being used to remove foul gas |
| CN108191115A (en) * | 2017-12-20 | 2018-06-22 | 中国石油天然气股份有限公司 | Method for treating ammonia nitrogen pollutants by recycling magnesium ammonium phosphate |
-
2019
- 2019-10-10 CN CN201910956903.XA patent/CN110721567A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4343765A (en) * | 1980-12-11 | 1982-08-10 | Georgia Tech Research Institute | Method for deodorizing and disinfecting air |
| CN1833730A (en) * | 2006-04-21 | 2006-09-20 | 王锡麟 | Public lavatory deodorant and prepn. thereof |
| CN204637987U (en) * | 2015-04-21 | 2015-09-16 | 南京朗洁环保科技有限公司 | A kind of hydrogen sulfide removal system based on photocatalysis spray |
| CN205461711U (en) * | 2016-01-29 | 2016-08-17 | 上海鸿来环保设备有限公司 | Static, photodissociation, compound all -in -one of catalysis |
| CN107020003A (en) * | 2016-01-29 | 2017-08-08 | 上海鸿来环保设备有限公司 | The Odor absorbers of lipid waste gas, peculiar smell baffle, the preparation method of the peculiar smell baffle, dry method technology of deodorization and its equipment |
| CN107115780A (en) * | 2017-04-25 | 2017-09-01 | 重庆安欣环保节能科技有限公司 | A kind of medicament and its deodorizing method for being used to remove foul gas |
| CN108191115A (en) * | 2017-12-20 | 2018-06-22 | 中国石油天然气股份有限公司 | Method for treating ammonia nitrogen pollutants by recycling magnesium ammonium phosphate |
Non-Patent Citations (1)
| Title |
|---|
| 《药物化学》编写组: "《药物化学》", 31 August 1980 * |
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