CN203862134U - Abnormal odor catalytic oxidizer for treating town household garbage - Google Patents
Abnormal odor catalytic oxidizer for treating town household garbage Download PDFInfo
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- CN203862134U CN203862134U CN201420262903.2U CN201420262903U CN203862134U CN 203862134 U CN203862134 U CN 203862134U CN 201420262903 U CN201420262903 U CN 201420262903U CN 203862134 U CN203862134 U CN 203862134U
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- urceolus
- foreign odor
- inner core
- catalytic
- catalytic oxidation
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Abstract
The utility model relates to an abnormal odor catalytic oxidizer for treating town household garbage, which comprises an intake and exhaust heat exchange structure, an electric heating device, a supported catalyst, a heat insulator and a temperature control device. The intake and exhaust heat exchange structure comprises an inner barrel and an outer barrel; the outer barrel is used as a shell; one end of the outer barrel is provided with a gas inlet and the other end of the outer barrel is provided with an end cover; spiral blades for gas flow guiding are arranged on the peripheral surface of the inner barrel; gas flow guide blades are radially arranged on the end face of the inner barrel; one end of the inner barrel is provided with an exhaust port and the other end of the inner barrel is provided with a ring-shaped end cover; the exhaust port extends out of the outer barrel; a catalytic oxidization chamber and a waste gas cooling passage are formed in the inner barrel; a fixed bracket is arranged on the end cover of the outer barrel; the electric heating device and the supported catalyst are arranged at intervals on the fixed bracket; the temperature control device comprises a controller and a thermocouple; the controller is connected with the electric heating device; the thermocouple is arranged in the catalytic oxidization chamber; the thermocouple is connected with the controller by a line. Utilization of the abnormal odor catalytic oxidizer for treating town household garbage can effectively solve the problem of environmental gas abnormal odor at household garbage treatment process points and in treatment workshops.
Description
Technical field
The utility model relates to a kind of catalytic oxidizer, especially relates to a kind of foreign odor catalytic oxidizer for application of city life garbage processing.
Background technology
The foreign odor harm of the collection of application of city life garbage, storage, transhipment, processing procedure is the technical barrier that allows people have a headache all the time.
House refuse complicated, mostly contain kitchen excess, content of organics is higher, and often there are a large amount of pathogen microorganisms and parasite and heavy metal element, its organic matter is corrupt under microbial action can go out various foreign odor gas by sustained release, these foreign odor gas ingredients are conventionally complicated, Main Ingredients and Appearance is roughly sulfur-containing compound, as hydrogen sulfide (gaseous state), methyl mercaptan (approximately 36 DEG C of boiling points), butyl mercaptan (approximately 122 DEG C of boiling points), tert-butyl mercaptan (approximately 64 DEG C of boiling points), propanethiol (approximately 68 DEG C of boiling points), propylene mercaptan (approximately 67 DEG C of boiling points), amyl hydrosulfide (approximately 123 DEG C of boiling points), beneze methane thiol (approximately 195 DEG C of boiling points), benzenethiol (approximately 168 DEG C of boiling points), p-benzyl mercaptan (approximately 43 DEG C of boiling points), sulfur dioxide (gaseous state), methyl disulfide (approximately 109 DEG C of boiling points), carbon disulfide (approximately-30 DEG C of boiling points) etc., nitrogen-containing compound, as ammonia (gaseous state), methylamine (approximately-6.8 DEG C of boiling points), ethamine (approximately 16.6 DEG C of boiling points), dimethylamine (approximately 6.9 DEG C of boiling points), trimethylamine (approximately-4 DEG C of boiling points), hydrazine (approximately 119 DEG C of boiling points), butylamine (approximately 44 DEG C of boiling points), Beta-alanine (approximately 198 DEG C of boiling points), beta-amino propyl alcohol (approximately 188 DEG C of boiling points), indoles etc., halogen and halogenated hydrocarbons, hydro carbons and aromatic hydrocarbon, oxygen-bearing organic matter, as alcohol, phenol, aldehyde, ketone etc.Wherein particularly evident with the toxicity of hydrogen sulfide, people is at 70～150mgH
2s/m
3in environment approximately 1 hour, there is irritation in respiratory tract and eyes, suck approximately 5 minutes after olfactory fatigue and do not hear that it is smelly; People is at about 300mgH
2s/m
3in environment approximately 8 minutes, there is acute irritation symptoms in eyes, causes that slightly for a long time pulmonary edema, bronchitis cause pneumonia, occurs that headache and dizziness feels sick; People is at 1000mgH
2s/m
3in environment can there is acute poisoning in the several seconds, and after accelerated breathing, respiratory paralysis is lethal.
Current, the method that solves house refuse foreign odor both at home and abroad can be summarized as: essence encapsulation method, and fragrant essence is covered foreign odor, but can not reduce foreign odor composition, local Dilution air method, arranges with blower fan exhausting dilution indoor stink or directly, still causes the pollution to external environment condition, solid matter absorption method, extract the just discharge after adsorbing with solid matters such as activated carbon, carbonate compound, zeolite, inorganic halides in special arrangement of foreign odor gas out with blower fan, with the degree that reduces externally to pollute, but effect depends on foreign odor molecular species, content, and active carbon etc. was easily because the little molecule foul odor poisoning of part was lost efficacy, Ozonation, i.e. Bian ozone oxidation H
2s and NH
3, effect depends on ozone concentration, but ozone itself just has a kind of stink, and ozone concentration reach 125PPM by harm people's health, affect surrounding environment, and the oxidizable inefficacy of the high-field electrode of ozone generator needs to regularly replace, effective microbe method, optimize and choose the high concentration that contains multiple occurring in nature, highly active efficacious microbial colony or yeast flora are cultivated, cloth is spread in house refuse, allow these microbial bacterias suppress to cause in rubbish the biochemistry activity of smelly microorganism, and utilize the nutrition of some stink thing as self, to reduce the rotten speed of rubbish and reeky foreign odor degree thereof, the current stable and reliability of the method still needs further to be studied, health effect international academic community to people also there is no final conclusion, and for be foreign odor source, instead of foreign odor molecule itself, inoperative to established foreign odor, also because of the installations and facilities of the large corrosion treatment of its solution acidic, plant extraction liquid catalytic oxidation, utilizes some natural botanical extraction liquids to destroy the character of hydrogen sulfide, mercaptan, ammonia, amine, aldehyde foul smell molecule, and through reaction, foul smell molecule generates the nontoxic product of odorless, and the method raw material sources are still limited and cost is still very high, negative pressure is collected into incinerator burning method, and the method is effective, but application often shown limitation, each operation point of domestic rubbish disposal process, during especially without large-scale incinerator and the operation point of dispersion and movement operation point be difficult to processing.
The said method application of house refuse deodorizing both at home and abroad has all obtained significant achievement, but resident and garbage disposal worker are still perplexed in the foreign odor of house refuse and harm, therefore, in the urgent need to a kind of rapidly and efficiently, house refuse foreign odor processing method and the treating apparatus of wide adaptability, solve the problem that affects of house refuse foreign odor from each operation point source and environment.
Utility model content
Technical problem to be solved in the utility model is that a kind of foreign odor catalytic oxidizer for application of city life garbage processing that can effectively eliminate the rubbish foreign odor on application of city life garbage processing workshop or treatment process point is provided.
The utility model solves the problems of the technologies described above taked technical scheme: a kind of foreign odor catalytic oxidizer for application of city life garbage processing, comprise intake and exhaust heat exchange structure, electrothermal device, carried catalyst, insulator and attemperating unit, described intake and exhaust heat exchange structure comprises inner core and urceolus, described urceolus is as housing, one end of described urceolus is provided with air inlet, the other end is provided with end cap, the periphery of described inner core is provided with the helical blade of air-flow guiding, the end-face diameter of described inner core is to being provided with air vane guide, one end of described inner core is provided with exhaust outlet, the other end is provided with annular end cap, described exhaust outlet extends to outside urceolus, it between described urceolus and inner core, is foreign odor gas preheating channel, described foreign odor gas preheating channel is communicated with air inlet, in described inner core, be provided with catalytic oxidation chamber, waste gas cooling duct, described catalytic oxidation chamber is communicated with foreign odor gas preheating channel, described waste gas cooling duct is communicated with catalytic oxidation chamber, the end cap of described urceolus is provided with fixed support, it is indoor that described fixed support stretches into catalytic oxidation, described electrothermal device and carried catalyst interval are arranged on fixed support and to be positioned at catalytic oxidation indoor, described attemperating unit comprises controller and thermocouple, described controller is located at outside housing and is connected with electrothermal device by circuit, described thermocouple is located on the end cap of urceolus and is stretched into that catalytic oxidation is indoor or to be directly located at catalytic oxidation indoor, described thermocouple is connected with controller by circuit.
Further, altogether center line of described inner core and urceolus, and inner core, urceolus are made up of two different cylinders of diameter respectively.Certainly, described urceolus and inner core can be designed to other versions such as square, and helical blade on inner core can be designed to be out of shape water conservancy diversion conduction vanes, and place, the waste gas cooling duct pipeline being connected with catalytic oxidation chamber can be designed to spiral heat exchange pipe coil.
Further, described air inlet place is provided with air inlet screen.Certainly, air inlet screen also can be arranged according to actual conditions, as air inlet screen being set in the negative-pressure dust suction hood being connected on the admission line being connected with air inlet or with admission line.
Further, be also provided with insulator, described insulator comprises heat reflection coatings layer and alumina silicate fibre carpet veneer, and described heat reflection coatings layer is positioned at housing inner side, and described alumina silicate fibre carpet veneer is positioned at hull outside and/or housing inner side.Certainly, also can select other general heat-insulating heat-preserving materials (as cellucotton etc.) that insulator is set in other way.
Further, described exhaust ports is provided with acid gas absorption plant.Certainly, also can in exhaust outlet connecting pipe, acid gas absorption plant be set.Described acid gas absorption plant is general oxysulfide and/or physics or the chemical absorbing device of sulfur and nitrogen oxides.
Further, described carried catalyst is that appendix has in rare earth element and manganese, iron, copper, nickel, cobalt, silver, titanium, niobium, vanadium, strontium, chromium, palladium, platinum, rhodium etc. one or more can promote asbestos or woven wire, rope, rod or the cellular solid of the catalytic elements that foreign odor molecular oxidation decomposes.Described catalytic elements also directly appendix on electrothermal device, form electrothermal device carried catalyst.
Described electrothermal device is general electrothermal device, silicon molybdenum electrothermal piece, resistance electrothermal part or the heating wire etc. of preferred generic.
Know-why of the present utility model:
1) generally very low for garbage disposal plant or the upper rubbish foreign odor poisonous and harmful molecule content concentration of operation point, extremely difficult stable ignition burns but the feature of oxidable decomposition, sets up controlled reliable and stable temperature field (being temperature field in oxidizing chamber).
2) for the molecule feature of rubbish foreign odor poisonous and harmful composition, adopt controllable temperature field catalytic oxidation principle, fast, thoroughly decomposing foreign odor molecule is simple oxide.
3) utilize intake and exhaust heat exchange structure, reclaim waste gas residual heat, preheating foreign odor gas, and form heat storage objectively with carried catalyst and electrothermal device, stop heat conducting and radiating with reliable insulator, the economy problems of the foreign odor that removes rubbish on the operation point of solution garbage disposal workshop or dispersion.
4) utilize electrothermal device and carried catalyst combination, solve catalyst sulfur poisoning problem.
5) can utilize the acid gas absorption plant of simple physical absorption absorption or chemical equation, be connected on waste gas outlet pipeline, remove decompose after contained limited amount SO in waste gas
2and NO
2.
The beneficial effects of the utility model:
1) can easily solve domestic rubbish disposal operation point above and even process the environmental gas foreign odor problem in workshop, dissolving the foreign odor gas harm of always perplexing for a long time resident and garbage disposal personnel.
2) non-secondary pollution, has no adverse effect to environment.
3) application is simple, good economy performance.
Brief description of the drawings
Fig. 1 is the structure cut-away view of the utility model embodiment-foreign odor catalytic oxidizer;
In figure: 1-intake and exhaust heat exchange structure, 2-catalytic oxidation chamber, 3-electrothermal device, 4-carried catalyst, 5-insulator, 6-housing, 7-air inlet screen, 9-air inlet, 10-foreign odor gas preheating channel, 11-exhaust outlet, 12-waste gas cooling duct, 13-controller, 14-thermocouple, 16-helical blade, 17-air vane guide, 18-fixed support, 19-annular end cap, 20-end cap.
detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in further detail.
With reference to accompanying drawing, the foreign odor catalytic oxidizer for application of city life garbage processing of the present embodiment, comprise intake and exhaust heat exchange structure 1, electrothermal device 3, carried catalyst 4, insulator 5 and attemperating unit, described intake and exhaust heat exchange structure 1 comprises inner core and urceolus, described urceolus is as housing 6, one end of described urceolus is provided with air inlet 9, the other end is provided with end cap 20, the periphery of described inner core is provided with the helical blade 16 of air-flow guiding, the end-face diameter of described inner core is to being provided with air vane guide 17, to improve heat exchanger effectiveness and stable inside and outside cylindrical shell relative position, one end of described inner core is provided with exhaust outlet 11, the other end is provided with annular end cap 19, described exhaust outlet 11 extends to outside urceolus, it between described urceolus and inner core, is foreign odor gas preheating channel 10, described foreign odor gas preheating channel 10 is communicated with air inlet 9, in described inner core, be provided with catalytic oxidation chamber 2, waste gas cooling duct 12, described catalytic oxidation chamber 2 is the catalytic oxidation decomposition space of foreign odor molecule, described catalytic oxidation chamber 2 is communicated with foreign odor gas preheating channel 10, described waste gas cooling duct 12 is communicated with catalytic oxidation chamber 2, the end cap 20 of described urceolus is provided with fixed support 18, and described fixed support 18 stretches in catalytic oxidation chamber 2, and described electrothermal device 3 and carried catalyst 4 intervals are arranged on fixed support 18, and are positioned at catalytic oxidation chamber 2, described attemperating unit comprises controller 13 and thermocouple 14, described controller 13 is located at outside housing 6 and is connected with electrothermal device 3 by circuit, described thermocouple 14 is located on the end cap 20 of urceolus and is stretched in catalytic oxidation chamber 2, and described thermocouple 14 is connected with controller 13 by circuit.
Altogether center line of described inner core and urceolus, and inner core, urceolus are made up of two different cylinders of diameter respectively.Certainly, described urceolus and inner core also can be designed to other versions such as square, and helical blade on inner core also can be designed to be out of shape water conservancy diversion conduction vanes, and place, the waste gas cooling duct pipeline being connected with catalytic oxidation chamber also can be designed to spiral heat exchange pipe coil.
Described thermocouple 14 also can directly be arranged in catalytic oxidation chamber 2.The effect of described electrothermal device 3 is preheatings and maintains catalytic oxidation chamber 2 temperature, and described carried catalyst 4 provides dynamic conditions for complete oxidation decomposes foreign odor molecule.
Air inlet 9 places of the present embodiment are also provided with air inlet screen 7.Certainly, described air inlet screen 7 also can be located in the negative-pressure dust suction hood being connected on the admission line being connected with air inlet 9 or with admission line, light refuse and the particle that may contain for removing the foreign odor gas of suction.
The present embodiment is also provided with insulator 5, described insulator 5 comprises heat reflection coatings layer and alumina silicate fibre carpet veneer, described heat reflection coatings layer is positioned at housing inner side, described alumina silicate fibre carpet veneer is positioned at hull outside, certainly also can be arranged at housing inner side, for stoping the heat conducting and radiating of oxidizing chamber 2 and reducing housing 6 surface temperatures.
Described in the present embodiment, in exhaust outlet 11 or exhaust outlet 11 connecting pipes, the further purifying gas of acid gas absorption plant can also be set.
Garbage disposal operation point foreign odor gas relies on blower fan suction work done, through air inlet screen 7 filtering light refuses, after particle, enter foreign odor gas preheating channel 10 from air inlet 9, interior through helical blade 16 water conservancy diversion at intake and exhaust heat exchange structure 1, enter end face air vane guide 17 water conservancy diversion, reenter next stage helical blade 16 water conservancy diversion, reentering end face air vane guide 17 water conservancy diversion progressively heats up, then enter in catalytic oxidation chamber 2 through the annular end cap 19 of inner core, through low middle temperature catalyst catalytic oxidation, be warming up to middle high temperature catalyst catalytic oxidation through electrothermal device 3 again, thoroughly be decomposed into simple oxide, out enter waste gas cooling duct 12 from catalytic oxidation chamber 2 subsequently, discharge through exhaust outlet 11, combustion gas can directly discharge or discharge after sour gas receiving system further purifies again, whole process can be utilized waste gas cooling duct 12 waste gas residual heats that catalytic oxidation chamber 2 discharges or utilize waste gas cooling duct 12 waste gas residual heats and catalytic oxidation chamber 2 temperature indirect foreign odor gases simultaneously.
Claims (5)
1. for the foreign odor catalytic oxidizer of application of city life garbage processing, it is characterized in that: comprise intake and exhaust heat exchange structure, electrothermal device, carried catalyst, insulator and attemperating unit, described intake and exhaust heat exchange structure comprises inner core and urceolus, described urceolus is as housing, one end of described urceolus is provided with air inlet, the other end is provided with end cap, the periphery of described inner core is provided with the helical blade of air-flow guiding, the end-face diameter of described inner core is to being provided with air vane guide, one end of described inner core is provided with exhaust outlet, the other end is provided with annular end cap, described exhaust outlet extends to outside urceolus, it between described urceolus and inner core, is foreign odor gas preheating channel, described foreign odor gas preheating channel is communicated with air inlet, in described inner core, be provided with catalytic oxidation chamber, waste gas cooling duct, described catalytic oxidation chamber is communicated with foreign odor gas preheating channel, described waste gas cooling duct is communicated with catalytic oxidation chamber, the end cap of described urceolus is provided with fixed support, it is indoor that described fixed support stretches into catalytic oxidation, described electrothermal device and carried catalyst interval are arranged on fixed support and to be positioned at catalytic oxidation indoor, described attemperating unit comprises controller and thermocouple, described controller is located at outside housing and is connected with electrothermal device by circuit, described thermocouple is located on the end cap of urceolus and is stretched into catalytic oxidation chamber or be directly located at catalytic oxidation indoor, described thermocouple is connected with controller by circuit.
2. the foreign odor catalytic oxidizer for application of city life garbage processing according to claim 1, is characterized in that: altogether center line of described inner core and urceolus, and inner core, urceolus are made up of two different cylinders of diameter respectively.
3. the foreign odor catalytic oxidizer for application of city life garbage processing according to claim 1 and 2, is characterized in that: described air inlet place is provided with air inlet screen.
4. the foreign odor catalytic oxidizer for application of city life garbage processing according to claim 1 and 2, it is characterized in that: be also provided with insulator, described insulator comprises heat reflection coatings layer and alumina silicate fibre carpet veneer, described heat reflection coatings layer is positioned at housing inner side, and described alumina silicate fibre carpet veneer is positioned at hull outside and/or housing inner side.
5. the foreign odor catalytic oxidizer for application of city life garbage processing according to claim 1 and 2, is characterized in that: described exhaust ports is provided with acid gas absorption plant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420262903.2U CN203862134U (en) | 2014-05-22 | 2014-05-22 | Abnormal odor catalytic oxidizer for treating town household garbage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420262903.2U CN203862134U (en) | 2014-05-22 | 2014-05-22 | Abnormal odor catalytic oxidizer for treating town household garbage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203862134U true CN203862134U (en) | 2014-10-08 |
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ID=51643125
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|---|---|---|---|
| CN201420262903.2U Active CN203862134U (en) | 2014-05-22 | 2014-05-22 | Abnormal odor catalytic oxidizer for treating town household garbage |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582229A (en) * | 2016-12-16 | 2017-04-26 | 广西红润化工科技有限公司 | Combined multistage waste gas treatment apparatus employing combined wet process and heating process treatment |
| CN107442553A (en) * | 2017-08-04 | 2017-12-08 | 怡然科技（深圳）有限公司 | Kitchen leftover treating apparatus |
| CN114534462A (en) * | 2022-03-18 | 2022-05-27 | 南京工程学院 | 3D printer exhaust treatment device |
-
2014
- 2014-05-22 CN CN201420262903.2U patent/CN203862134U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582229A (en) * | 2016-12-16 | 2017-04-26 | 广西红润化工科技有限公司 | Combined multistage waste gas treatment apparatus employing combined wet process and heating process treatment |
| CN107442553A (en) * | 2017-08-04 | 2017-12-08 | 怡然科技（深圳）有限公司 | Kitchen leftover treating apparatus |
| CN107442553B (en) * | 2017-08-04 | 2023-01-10 | 骧腾科技(深圳)有限公司 | Kitchen waste treatment equipment |
| CN114534462A (en) * | 2022-03-18 | 2022-05-27 | 南京工程学院 | 3D printer exhaust treatment device |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20161111 Address after: 410205 Hunan province high tech Development Zone Changsha Wenxuan Road No. 27 Lu Valley Yuyuan D3-101 building two floor Patentee after: CHANGSHA ZICHEN TECHNOLOGY DEVELOPMENT CO., LTD. Address before: 410013 Hunan province high tech Development Zone C2 group Binjiang fortune Silicon Valley building, room 5, building 510, room Patentee before: Yin Xiaolin |