CN105289176A - Simple garbage incinerator tail gas filtering device for farms - Google Patents
Simple garbage incinerator tail gas filtering device for farms Download PDFInfo
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- CN105289176A CN105289176A CN201510725568.4A CN201510725568A CN105289176A CN 105289176 A CN105289176 A CN 105289176A CN 201510725568 A CN201510725568 A CN 201510725568A CN 105289176 A CN105289176 A CN 105289176A
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- flue gas
- flow tank
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Abstract
The invention discloses a simple garbage incinerator tail gas filtering device for farms. The device is characterized by comprising a chamber settling box, wherein one end of the settling box is connected to a flue gas discharge outlet of an incinerator; a flue gas outlet is formed in the other end of the settling box; a spray pipe is arranged in the settling box; and a high-pressure mist spray head is arranged on the spray pipe. A liquid settling agent is sprinkled into the settling box by virtue of the high-pressure mist spray head, the temperature of the liquid settling agent is controlled to be 65 DEG C, and mist spraying is performed in an uninterrupted manner, so that harmful flue gas in the settling box is reacted and settled, and up-to-standard release of the flue gas is realized. The traditional filtering equipment is transformed, the inner structure is rearranged, the filter settling agent is improved by virtue of experiment innovation, and the tail gases generated by waste incineration are treated, so that pollutants in the discharged tail gases are eliminated, and the device is environmentally friendly to atmosphere and harmless to a human body.
Description
Technical field
The present invention relates to garbage incinerating tail gas processing technology field, be specifically related to a kind of farm simple waste tail gas from incinerator filter.
Background technology
Incineration treatment of garbage is placed in incinerator by rubbish to burn, and discharges heat energy, and waste heat recovery can heat supply or generating, discharges after gas cleaning, and a small amount of residual residue is discharged landfill or made other purposes.Incineration treatment technology feature is that treating capacity is large, to subtract capacitive good, thoroughly innoxious, and has energy recovery effect.Therefore, effective processing mode that burning disposal is innoxious, minimizing and resource is carried out to rubbish.
Purified by purification facility after the fume emission of incineration firing, because conventional rubbish incinerator adopts merely water tank to filter, weak effect, gas discharging is not up to standard.
Summary of the invention
It is simple that technical problem to be solved by this invention is to provide a kind of scrap build, good in economic efficiency farm simple waste tail gas from incinerator filter.
Technical problem to be solved by this invention realizes by the following technical solutions:
A kind of farm simple waste tail gas from incinerator filter, comprise one and there is cavity volume flow tank, described flow tank one end is connected to the fume emission mouth of incinerator, the flow tank other end is provided with flue gas discharge opening, shower is provided with in described flow tank, described shower is provided with high pressure Fine spray shower nozzle, by high pressure Fine spray shower nozzle to spraying liquid sedimentation agent in flow tank, the temperature of liquid sedimentation agent controls at 65 DEG C, continual mode is adopted to spray, the harmful smoke through flow tank is made to carry out reaction sedimentation, then qualified discharge;
Described flue gas discharge opening is provided with smoke filtration Nomex, carries out filtration treatment further to the flue gas after sedimentation.
Described liquid sedimentation agent is made up of the component of following parts by weight: the tert-butyl alcohol 100 parts, magnetized drinking water 10 parts, shitosan 2 parts, saponin 1 part, watermelon polysaccharide 0.5 part, Cardia Salt 3 parts, wheat oligopeptide 0.5 part, lutein ester 0.5 part, Oman holder flavones 0.04 part, baicalin 0.2 part, softening agent 1.5 parts, water-base resin 2 parts, cationic starch 2.5 parts, 2 parts, urea, 0.06 part, sodium sulphate, rare earth oxide 0.06 part;
Described smoke filtration Nomex is impregnated with gas filtration agent, and described gas filtration agent is made up of the component of following parts by weight: magnetized drinking water 80 parts, nanometer silicon carbide 1.2 parts, curcumin 0.05 part, carbon nano-fiber 2 parts, hydrolyzed silk protein 0.5 part, zytase 0.05 part, HPMC 0.5 part, 0.6 part, antistatic additive, amorphous silica particulate 1.5 parts, inorganic silica gel 2 parts, sodium pyrophosphate 2 parts, nylon fiber 2 parts;
Described amorphous silica particulate adopts the amorphous silica particulate of D < 15nm.
For improving the physicochemical property of described smoke filtration Nomex further, smoke filtration Nomex need after gas filtration agent dipping drying and processing again, smoke filtration Nomex is 0.7m/min by the speed that gas filtration agent is flooded, and bake out temperature is 100 DEG C ~ 120 DEG C, and the time is 60min.
The invention has the beneficial effects as follows: the present invention transforms traditional filtering equipment, again layout is carried out to internal structure, and innovation improves filtration sedimentation agent by experiment, the tail gas produced for waste incineration processes, make the tail gas after discharging without any pollutant, to air environmental protection, to human body fanout free region.
Accompanying drawing explanation
Fig. 1 is structure chart of the present invention.
Detailed description of the invention
The technological means realized to make the present invention, creation characteristic, reaching object and effect is easy to understand, below in conjunction with concrete diagram, setting forth the present invention further.
As shown in Figure 1, a kind of farm simple waste tail gas from incinerator filter, comprise one and there is cavity volume flow tank 1, flow tank 1 one end is connected to the fume emission mouth 2 of incinerator, flow tank 1 other end is provided with flue gas discharge opening 3, shower 4 is provided with in flow tank 1, shower 4 is provided with high pressure Fine spray shower nozzle 5, by high pressure Fine spray shower nozzle 5 to spraying liquid sedimentation agent in flow tank 1, the temperature of liquid sedimentation agent controls at 65 DEG C, adopt continual mode to spray, make the harmful smoke through flow tank 1 carry out reaction sedimentation, then qualified discharge; Flue gas discharge opening 3 is provided with smoke filtration Nomex 6, carries out filtration treatment further to the flue gas after sedimentation.
Described liquid sedimentation agent is made up of the component of following parts by weight: the tert-butyl alcohol 100 parts, magnetized drinking water 10 parts, shitosan 2 parts, saponin 1 part, watermelon polysaccharide 0.5 part, Cardia Salt 3 parts, wheat oligopeptide 0.5 part, lutein ester 0.5 part, Oman holder flavones 0.04 part, baicalin 0.2 part, softening agent 1.5 parts, water-base resin 2 parts, cationic starch 2.5 parts, 2 parts, urea, 0.06 part, sodium sulphate, rare earth oxide 0.06 part;
Described smoke filtration Nomex 6 is impregnated with gas filtration agent, and described gas filtration agent is made up of the component of following parts by weight: magnetized drinking water 80 parts, nanometer silicon carbide 1.2 parts, curcumin 0.05 part, carbon nano-fiber 2 parts, hydrolyzed silk protein 0.5 part, zytase 0.05 part, HPMC 0.5 part, 0.6 part, antistatic additive, amorphous silica particulate 1.5 parts, inorganic silica gel 2 parts, sodium pyrophosphate 2 parts, nylon fiber 2 parts;
Described amorphous silica particulate adopts the amorphous silica particulate of D < 15nm.
For improving the physicochemical property of described smoke filtration Nomex further, smoke filtration Nomex need after gas filtration agent dipping drying and processing again, smoke filtration Nomex is 0.7m/min by the speed that gas filtration agent is flooded, and bake out temperature is 100 DEG C ~ 120 DEG C, and the time is 60min.
More than show and describe general principle of the present invention and principal character and advantage of the present invention.The technical staff of the industry should understand; the present invention is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and these changes and improvements all fall in the claimed scope of the invention.Application claims protection domain is defined by appending claims and equivalent thereof.
Claims (3)
1. a farm simple waste tail gas from incinerator filter, it is characterized in that, comprise one and there is cavity volume flow tank, described flow tank one end is connected to the fume emission mouth of incinerator, the flow tank other end is provided with flue gas discharge opening, shower is provided with in described flow tank, described shower is provided with high pressure Fine spray shower nozzle, by high pressure Fine spray shower nozzle to spraying liquid sedimentation agent in flow tank, the temperature of liquid sedimentation agent controls at 65 DEG C, adopt continual mode to spray, make the harmful smoke through flow tank carry out reaction sedimentation, then qualified discharge.
2. farm according to claim 1 simple waste tail gas from incinerator filter, is characterized in that: described flue gas discharge opening is provided with smoke filtration Nomex, carries out filtration treatment further to the flue gas after sedimentation.
3. farm according to claim 2 simple waste tail gas from incinerator filter, it is characterized in that: described smoke filtration Nomex is impregnated with gas filtration agent, described gas filtration agent is made up of the component of following parts by weight: magnetized drinking water 80 parts, nanometer silicon carbide 1.2 parts, curcumin 0.05 part, carbon nano-fiber 2 parts, hydrolyzed silk protein 0.5 part, zytase 0.05 part, HPMC 0.5 part, 0.6 part, antistatic additive, amorphous silica particulate 1.5 parts, inorganic silica gel 2 parts, sodium pyrophosphate 2 parts, nylon fiber 2 parts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510725568.4A CN105289176B (en) | 2015-10-28 | 2015-10-28 | Farm simple waste tail gas from incinerator defecator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510725568.4A CN105289176B (en) | 2015-10-28 | 2015-10-28 | Farm simple waste tail gas from incinerator defecator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105289176A true CN105289176A (en) | 2016-02-03 |
| CN105289176B CN105289176B (en) | 2017-03-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510725568.4A Expired - Fee Related CN105289176B (en) | 2015-10-28 | 2015-10-28 | Farm simple waste tail gas from incinerator defecator |
Country Status (1)
| Country | Link |
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| CN (1) | CN105289176B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107670442A (en) * | 2017-09-07 | 2018-02-09 | 蚌埠市安华工贸有限公司 | Tail gas from incinerator discharge fume extractor |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2268188Y (en) * | 1996-07-01 | 1997-11-19 | 朱国华 | Device for treating house refuse |
| CN2462252Y (en) * | 2001-01-10 | 2001-11-28 | 武进市常宁环保设备有限公司 | Heat decomposing garbage incinerator |
| CN2697473Y (en) * | 2004-03-20 | 2005-05-04 | 周如俊 | Refuse incinerator |
| CN202682996U (en) * | 2012-07-31 | 2013-01-23 | 马鞍山仰望仁义锅炉有限公司 | Spraying box for water curtain dust collector |
| CN104474823A (en) * | 2014-11-27 | 2015-04-01 | 界首市东威塑业有限公司 | Tail gas environmental protection treatment device in granulating process of modified plastic granules |
| CN104728845A (en) * | 2015-03-19 | 2015-06-24 | 粟保成 | Pollution-free and harmless household garbage incinerator |
| CN104857796A (en) * | 2015-04-22 | 2015-08-26 | 安徽浩瀚环保科技有限公司 | Plastic granulator dust environmental treatment apparatus |
-
2015
- 2015-10-28 CN CN201510725568.4A patent/CN105289176B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2268188Y (en) * | 1996-07-01 | 1997-11-19 | 朱国华 | Device for treating house refuse |
| CN2462252Y (en) * | 2001-01-10 | 2001-11-28 | 武进市常宁环保设备有限公司 | Heat decomposing garbage incinerator |
| CN2697473Y (en) * | 2004-03-20 | 2005-05-04 | 周如俊 | Refuse incinerator |
| CN202682996U (en) * | 2012-07-31 | 2013-01-23 | 马鞍山仰望仁义锅炉有限公司 | Spraying box for water curtain dust collector |
| CN104474823A (en) * | 2014-11-27 | 2015-04-01 | 界首市东威塑业有限公司 | Tail gas environmental protection treatment device in granulating process of modified plastic granules |
| CN104728845A (en) * | 2015-03-19 | 2015-06-24 | 粟保成 | Pollution-free and harmless household garbage incinerator |
| CN104857796A (en) * | 2015-04-22 | 2015-08-26 | 安徽浩瀚环保科技有限公司 | Plastic granulator dust environmental treatment apparatus |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107670442A (en) * | 2017-09-07 | 2018-02-09 | 蚌埠市安华工贸有限公司 | Tail gas from incinerator discharge fume extractor |
| CN107670442B (en) * | 2017-09-07 | 2020-04-21 | 蚌埠市安华工贸有限公司 | Smoke exhaust device for exhaust emission of incinerator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105289176B (en) | 2017-03-29 |
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Granted publication date: 20170329 Termination date: 20211028 |