CN202359072U - Refuse cracking-purifying equipment - Google Patents
Refuse cracking-purifying equipment Download PDFInfo
- Publication number
- CN202359072U CN202359072U CN2011204688031U CN201120468803U CN202359072U CN 202359072 U CN202359072 U CN 202359072U CN 2011204688031 U CN2011204688031 U CN 2011204688031U CN 201120468803 U CN201120468803 U CN 201120468803U CN 202359072 U CN202359072 U CN 202359072U
- Authority
- CN
- China
- Prior art keywords
- gas
- cracking
- heater
- rubbish
- ultra
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000005336 cracking Methods 0.000 claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 239000010813 municipal solid waste Substances 0.000 claims description 44
- 238000010521 absorption reaction Methods 0.000 claims description 43
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 26
- 239000003513 alkali Substances 0.000 claims description 19
- 238000001179 sorption measurement Methods 0.000 claims description 18
- 239000007787 solid Substances 0.000 claims description 11
- 239000002893 slag Substances 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000003344 environmental pollutant Substances 0.000 abstract description 4
- 231100000719 pollutant Toxicity 0.000 abstract description 4
- 230000001502 supplementing effect Effects 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 99
- 238000000034 method Methods 0.000 description 28
- 238000000746 purification Methods 0.000 description 12
- 238000004659 sterilization and disinfection Methods 0.000 description 9
- 239000000428 dust Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 150000003839 salts Chemical class 0.000 description 8
- 238000007599 discharging Methods 0.000 description 7
- 229920006395 saturated elastomer Polymers 0.000 description 7
- 230000001954 sterilising effect Effects 0.000 description 7
- 238000001035 drying Methods 0.000 description 6
- 230000007935 neutral effect Effects 0.000 description 6
- 231100000614 poison Toxicity 0.000 description 6
- 230000007096 poisonous effect Effects 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 238000000197 pyrolysis Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000009931 harmful effect Effects 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 150000002013 dioxins Chemical class 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000002309 gasification Methods 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000005431 greenhouse gas Substances 0.000 description 3
- 239000002906 medical waste Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 239000000809 air pollutant Substances 0.000 description 2
- 231100001243 air pollutant Toxicity 0.000 description 2
- 238000003776 cleavage reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 230000007017 scission Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 238000004380 ashing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000010834 chemotherapy waste Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002901 radioactive waste Substances 0.000 description 1
- 239000003206 sterilizing agent Substances 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Images
Landscapes
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses refuse cracking-purifying equipment which is low in operation cost, good in purifying treatment effect, low in energy consumption and free from pollutant emission. The refuse cracking-purifying equipment disclosed by the utility model comprises a shell, a feeding-conveying device, a cracking furnace body, a gas absorbing tank, an ultrahigh-frequency power supply host machine, an alkaline liquid container, and a gas purifying-adsorbing tower, wherein the feeding-conveying device is connected with the feed port of the cracking furnace body; a gas cracking component is connected between the cracking furnace body and the gas absorbing tank; the gas cracking component and the cracking furnace body are further connected with an ultrahigh-frequency electromagnetic heater which is electrically connected with the ultrahigh-frequency power supply host machine; the gas absorbing tank is connected with an alkaline liquid supplementing tank, a high-density purifier and a gas-liquid separator respectively; both of the gas absorbing tank and the alkaline liquid supplementing tank are connected with the alkaline liquid container; and the gas-liquid separator is connected with the gas purifying-adsorbing tower via a fan. The refuse cracking-purifying equipment disclosed by the utility model can be widely applied to the field of refuse purifying equipment.
Description
Technical field
The utility model relates to a kind of rubbish cracking treating plant.
Background technology
Existing comparatively typical treatment process mainly contains following several kinds:
1. autoclaving: investment is supported, and process cost is low, is easy to detect see that residue danger is lower, and sterilisation effect is good, and suitable process range is wider.The shortcoming of this kind method is that volume and outward appearance do not have to change basically, and air pollutant emission is arranged, and is prone to produce foul smell, can not handle materials such as formaldehyde.
2. microwave treatment method: volume significantly reduces, and rubbish unmakes effective; System is airtight fully, environmental pollution is very little; Fully automated, easy handling.The shortcoming of this kind method is to build and the running cost height; It is bad to handle the back weight loss effect, can frowziness.
3. chemical disinfection: processing unit and simple to operation, good deodorization effect, sterilizing process is rapid; One-time investment is few, and working cost is low.The shortcoming of this kind method is not to be suitable for to handle chemotherapy waste, radioactive waste, volatilization and half volatile organic compound.Poor processing effect, processing costs is high and not thorough.
4. pyrolysis processing method: temperature is lower, flames of anger combustion processes, and heavy metals etc. mostly maintain the original state among residue, have the effect that suppresses generation of dioxin.The shortcoming of this kind method is that garbage decomposition is not thorough with sterilization, and energy consumption is big.
5. high temperature incineration facture: volume and weight significantly reduces, and rubbish unmakes obviously; Be suitable for all type of wastes and large-scale application; Stable, sterilization and pollutant removal are good; The recyclable utilization of potential heat energy; The technology comparative maturity.The shortcoming of this kind method is to build and the running cost height, and atmospheric pollution is serious, produces obnoxious flavoures such as dioxin, needs the perfect exhaust gas purification system of configuration, and end slag and flying dust have hazardness.And, can cause the secondary pollution in loading, unloading, carrying and the transportation away from germ dangerous matter sources such as harmful poisonous.
6. sanitary landfill facture: technology is simpler, can handle a large amount of clinical wastes.The shortcoming of this kind method is to need sterilization before the landfill, and refuse is compatible few, and the landfill construction investment is big, need take a large amount of soils, produces a large amount of gases and volatile organic matter, need carry out long term monitoring to soil and underground water.
7. xeothermic pulverizing sterilization: sterilization is fast, subtracts and holds 80%, and construction and running cost are low, and the rubbish after the processing can carry out landfill disposal or comprehensive utilization, and treating processes need not adopt sterilizing agent.The shortcoming of this kind method is to carry out pre-treatment such as fragmentation, and sterilisation effect is not obvious, and air pollutant emission is arranged, and is prone to produce foul smell.
In sum, existing garbage treating process and the treatment facility that adopted exist that running cost is higher, treatment effect is relatively poor, energy consumption is big, technological deficiencies such as pollutant emission are arranged.
The utility model content
The utility model technical problem to be solved is the deficiency that overcomes prior art, provides that a kind of running cost is lower, purifying treatment is effective, energy consumption is less, the rubbish cracking treating plant of non-pollutant discharge.
The technical scheme that the said rubbish cracking of the utility model treating plant is adopted is: said rubbish cracking treating plant comprises housing, e Foerderanlage feeds intake; Pyrolyzer body of heater, gas absorption jar, ultra-high frequency power supply main frame, alkali liquor container, gas sweetening adsorption tower are installed in the said housing; Said pyrolyzer body of heater top and the bottom are provided with opening for feed and solid slag drain respectively; The said e Foerderanlage that feeds intake is connected with the opening for feed of said pyrolyzer body of heater; Be connected with gas cracking parts between said pyrolyzer body of heater and the gas absorption jar, said pyrolyzer body of heater also is connected with the ultra-high frequency electromagnetic heater, and said gas cracking parts are connected with the ultra-high frequency electromagnetic heater; Said ultra-high frequency electromagnetic heater all is electrically connected with said ultra-high frequency power supply main frame; Said gas absorption jar is connected with respectively mends alkali liquid tank, high-density cleaner, gas-liquid separator, and said gas absorption jar all is connected with said lye tank through NaOH solution circulating pump with the benefit alkali liquid tank, and said high-density cleaner is provided with the drain of purifying waste water; Said gas-liquid separator is connected with said gas sweetening adsorption tower through blower fan, and said gas sweetening adsorption tower is provided with the clean gas drain.
Optimally, be provided with the transfusion force (forcing) pump between said gas absorption jar and the said high-density cleaner.
Be provided with the one-level accurate filter between said blower fan and the said gas sweetening adsorption tower.
The clean gas drain place of said gas sweetening adsorption tower is provided with the secondary accurate filter.
The said e Foerderanlage that feeds intake comprises rubbish collection bucket and travelling belt.Said outside also is equipped with the work staircase.
The technical scheme that said rubbish cracking purification process technique is adopted is: said rubbish cracking purification process technique may further comprise the steps:
Step 1: step feeds intake; Rubbish compiles the back and is delivered to the opening for feed of said pyrolyzer body of heater by the e Foerderanlage that feeds intake, and drops in the said pyrolyzer body of heater; Step 2: solid cleavage step; The heating of said pyrolyzer body of heater is the 380V alternating-current that attracts from housing through ultra-high frequency power supply main frame; Insert the ultra-high frequency electromagnetic heater and make frequency be elevated to the 200-600 hertz, and generation eddy current heat carries out heat to solid refuse in the said pyrolyzer body of heater; The pyrolyzer body of heater carries out Pintsch process to rubbish under the condition of airtight, oxygen deprivation, at temperature 850-1000 ℃, and the rapid carbon charing of rubbish, the rubbish of carbon charing is discharged from said solid slag drain; Step 3: gas delivery step; Rubbish in the step 2 gets into said gas heating parts at the gas that said pyrolyzer body of heater internal cause Pintsch process produces; And in said gas heating parts, heat once more, the gas of Pintsch process, drying, destructive distillation and gasification is warming up to 1100-1300 ℃ rapidly in said gas heating parts in said pyrolyzer body of heater, makes the further cracking of gas; Eliminate poisonous, obnoxious flavoures such as Dioxins; Get into said gas absorption jar then, Pintsch gas is through the chilling of gas absorption jar, absorb, in and the temperature in the high-temperature gas, peculiar smell, water vapor, sour gas; Product after the neutralization is a neutral salt liquid; Salt liquid is when pH value reaches 6-8 in the gas absorption jar, is evacuated to the high-density cleaner through the transfusion force (forcing) pump and separates out and purify moisture content and discharge the regular collection and treatment of solid salt; Step 4: gas cleanup step; According to the chilling of step 3 Pintsch gas through the gas absorption jar; Be not absorbed, neutral saturated gas and dust cloud; Secondary alkali lye spray in the gas absorption jar extracts the gas in pyrolyzer body of heater, gas absorption jar, the gas-liquid separator by blower fan, and discharging through the one-level accurate filter is the clean gas of 0.03 μ; Be delivered to the gas sweetening adsorption tower; Further by the micro-dust granules of leading portion absorption and saturated gas such as H2, CO2, N2 and the peculiar smell of filtration drying, discharging through the secondary accurate filter is not the clean gas of 0.001 μ again, need not chimney and discharges in absorption.
Said rubbish cracking purification process technique also comprises the gas-liquid separation step, through the gas-liquid separator installed between said gas absorption jar and the blower fan with the moist saturated gas that is not adsorbed in the said gas absorption jar such as H2, CO2, N2 and liquid separation.
The beneficial effect of the utility model is: the utility model is under high temperature (850～1200 ℃) environment of fully-closed, negative pressure, oxygen deprivation; Decompose all kinds of materials in the medical waste; Experience different stepss such as drying, destructive distillation and gasification successively; Separate out moisture in dry, destructive distillation stage, be cracked into gases such as H2, CO, CO2 and CH4 at gasifying stage, and through physics, chemical technology purifying treatment; Prevent the generation and the discharging of poisonous and harmfuls such as Dioxins, CO2, NOX, N2 and greenhouse gases, the complete carbon ashing of slag.Sewage is through purification, and by the first discharge standard requirement, discharging reaches harmless day smokeless, nontoxic, harmless, tasteless purification target.The utility model provides effectively that a kind of energy expenditure is low, rubbish unmakes obviously, sterilization is fast, subtract and hold effective garbage purification equipment and the rubbish cracking purification process technique of decrement.
The utility model can be placed near the dangerous generation sources such as disease carrying germ, virus; At any time handle with producing; Three waste discharge problems such as noiselessness, no sewage, no dust can not pollute promptly energy-conservation environmental protection again to atmosphere and environment; Can eliminate the feared state of mind of dangerous matter sources such as people's disease carrying germ, virus, can prevent that rubbish is because of the secondary pollution in loading, unloading, carrying and the transportation simultaneously.The source can take place at pollutent and directly install and use in the rubbish cracking treating plant that the utility model provides; Particularly directly install and use in the place that produces medical waste; Can originate from certainly source of pollution and to go out; Can remove from the pollutent transhipment course of conveying the pollution of environment, avoid causing secondary pollution, produced pollution thing can obtain fast purification on the spot and handle.
Description of drawings
Fig. 1 is the floor plan synoptic diagram of the utility model;
Fig. 2 is the side portion structure synoptic diagram of the utility model;
Fig. 3 is the internal structure synoptic diagram of the utility model;
Fig. 4 is that the inside of the utility model connects synoptic diagram;
Fig. 5 is the FB(flow block) of the clean treatment process of the said rubbish cracking of the utility model.
Embodiment
Like Fig. 1, Fig. 2, Fig. 3, shown in Figure 4; The said rubbish cracking of the utility model treating plant comprises housing 21, e Foerderanlage feeds intake; Pyrolyzer body of heater 1, gas absorption jar 7, ultra-high frequency power supply main frame 15, alkali liquor container 18, gas sweetening adsorption tower 13 are installed in the said housing 21; Said pyrolyzer body of heater 1 is used for rubbish such as Pintsch process is done, moist medical treatment, life, the rubbish component is decomposed fully, vertical, side formula or horizontal that its external form can be divided into; Said pyrolyzer body of heater 1 top and the bottom are provided with opening for feed and solid slag drain 2 respectively; The said e Foerderanlage that feeds intake is connected with the opening for feed of said pyrolyzer body of heater 1; Be connected with gas cracking parts 3 between said pyrolyzer body of heater 1 and the gas absorption jar 7; Said pyrolyzer body of heater 1 also is connected with ultra-high frequency electromagnetic heater 16, and said gas cracking parts 3 are connected with ultra-high frequency electromagnetic heater 17, and said ultra-high frequency electromagnetic heater 16,17 all is electrically connected with said ultra-high frequency power supply main frame 15; Said gas absorption jar 7 is connected with respectively mends alkali liquid tank 6, high-density cleaner 9, gas-liquid separator 10; Said gas absorption jar 7 with mend alkali liquid tank 6 and all be connected with said alkali liquor container 18 through NaOH solution circulating pump 5, said NaOH solution circulating pump 5 can replenish alkali lye in said benefit alkali liquid tank 6 for use, the while can be in said gas absorption jar 7 the alkali lye cycle heat exchange; Guarantee chemical reaction uniformity in the gas absorption jar 7; Replenish alkali lye by said benefit alkali liquid tank 6 to said gas absorption jar 7, can absorb the overflow liquid that the moisture content because of the water vapor condensation of gas absorption jar 7 hyperabsorptions causes simultaneously, said gas absorption jar 7 is made up of alkali lye storehouse, salt slag strainer, cooling sump; Said gas absorption jar 7 main effects are sour gas, dust and the peculiar smell in the rapid absorbing high temp gas; And poisonous and harmful and greenhouse gases such as CO2, NOX, N2, eliminate the discharging of poisonous and harmful and greenhouse gases, said high-density cleaner 9 is provided with the drain of purifying waste water; Said high-density cleaner 9 is used to purify neutral salt liquid; Overflow clean moisture content through the high density filter pipe, said gas-liquid separator 10 is connected with said gas sweetening adsorption tower 13 through blower fan 11, and said blower fan 11 can adopt roots blower; Said gas sweetening adsorption tower 13 is provided with the clean gas drain, and said gas sweetening adsorption tower 13 further adsorbs not by the micro-dust granules of leading portion absorption and saturated gas such as H2, CO2, N2 and the peculiar smell of filtration drying.
Be provided with transfusion force (forcing) pump 8 between said gas absorption jar 7 and the said high-density cleaner 9, can quicken the saline solution of neutral pH value 6 ~ 8 in the said gas absorption jar 7 is delivered to high-density cleaner 9 through said transfusion force (forcing) pump 8.
Be provided with one-level accurate filter 12 between said blower fan 11 and the said gas sweetening adsorption tower 13, it mainly acts on is further refinement gas, and expellant gas is the clean gas of 0.03 μ.
The clean gas drain place of said gas sweetening adsorption tower 13 is provided with secondary accurate filter 14, and through said secondary accurate filter 14 further refinement gases, and expellant gas is the clean gas of 0.001 μ, need not chimney and discharges.
The said e Foerderanlage that feeds intake comprises rubbish collection bucket 22 and travelling belt 23.In practical application, also can adopt type of transmission such as chain or rail mounted.Said housing 22 outsides also are equipped with work staircase 24.
Like Fig. 4, shown in Figure 5, said rubbish cracking purification process technique may further comprise the steps:
Step 1: step feeds intake; Rubbish compiles the back and is delivered to the opening for feed of said pyrolyzer body of heater 1 by the e Foerderanlage that feeds intake, and drops in the said pyrolyzer body of heater 1; Step 2: solid cleavage step; The heating of said pyrolyzer body of heater 1 is the 380V alternating-current that attracts from housing through ultra-high frequency power supply main frame 5; Get into ultra-high frequency electromagnetic heater 16,17 and make frequency be elevated to the 200-600 hertz, and generation eddy current heat carries out heat to solid refuse in the said pyrolyzer body of heater 1; Pyrolyzer body of heater 1 carries out Pintsch process to rubbish under the condition of airtight, oxygen deprivation, at temperature 850-1000 ℃, and the rapid carbon charing of rubbish, the rubbish of carbon charing is discharged from said solid slag drain 2; Step 3: gas delivery step; Rubbish in the step 2 gets into said gas heating parts 3 at the gas that said pyrolyzer body of heater 1 internal cause Pintsch process produces; And in said gas heating parts 3, heat once more, the gas of Pintsch process, drying, destructive distillation and gasification is warming up to 1100-1300 ℃ rapidly in said gas heating parts 3 in said pyrolyzer body of heater 1, makes the further cracking of gas; Eliminate poisonous, obnoxious flavoures such as Dioxins; Get into said gas absorption jar 7 then, Pintsch gas is through the chilling of gas absorption jar 7, absorb, in and the temperature in the high-temperature gas, peculiar smell, water vapor, sour gas; Product after the neutralization is a neutral salt liquid; Salt liquid is when pH value reaches 6-8 in gas absorption jar 7, is evacuated to high-density cleaner 9 through transfusion force (forcing) pump 8 and separates out and purify moisture content and discharge the regular collection and treatment of solid salt; Step 4: gas cleanup step; According to the chilling of step 3 Pintsch gas through gas absorption jar 7; Be not absorbed, neutral saturated gas and dust cloud, the secondary alkali lye spray in gas absorption jar 7 extracts the gas in pyrolyzer body of heater 1, gas absorption jar 7, the gas-liquid separator 10 by blower fan 11; Discharging through one-level accurate filter 12 is the clean gas of 0.03 μ; Be delivered to gas sweetening adsorption tower 13, further absorption is not by the micro-dust granules of leading portion absorption and saturated gas such as H2, CO2, N2 and the peculiar smell of filtration drying, and discharging through secondary accurate filter 14 is the clean gas of 0.001 μ again; Need not chimney, can directly discharge.
Said rubbish cracking purification process technique also comprises the gas-liquid separation step, through the gas-liquid separator 14 installed between said gas absorption jar 7 and the blower fan 11 with the 7 moist saturated gas such as H2, CO2, N2 and the liquid separation that are not adsorbed in the said gas absorption jar.
The utility model can be widely used in the garbage purification apparatus field.
Claims (6)
1. rubbish cracking treating plant; Comprise housing (21), e Foerderanlage feeds intake; It is characterized in that: pyrolyzer body of heater (1), gas absorption jar (7), ultra-high frequency power supply main frame (15), alkali liquor container (18), gas sweetening adsorption tower (13) are installed in the said housing (21); Said pyrolyzer body of heater (1) top and the bottom are provided with opening for feed (25) and solid slag drain (2) respectively; The said e Foerderanlage that feeds intake is connected with the opening for feed of said pyrolyzer body of heater (1); Be connected with gas cracking parts (3) between said pyrolyzer body of heater (1) and the gas absorption jar (7); Said pyrolyzer body of heater (1) also is connected with ultra-high frequency electromagnetic heater (16); Said gas cracking parts (3) are connected with ultra-high frequency electromagnetic heater (17), and said ultra-high frequency electromagnetic heater (16), (17) all are electrically connected with said ultra-high frequency power supply main frame (15), and said gas absorption jar (7) is connected with respectively mends alkali liquid tank (6), high-density cleaner (9), gas-liquid separator (10); Said gas absorption jar (7) all is connected with said alkali liquor container (18) through NaOH solution circulating pump (5) with benefit alkali liquid tank (6); Said high-density cleaner (9) is provided with the drain of purifying waste water, and said gas-liquid separator (10) is connected with said gas sweetening adsorption tower (13) through blower fan (11), and said gas sweetening adsorption tower (13) is provided with the clean gas drain.
2. a kind of rubbish cracking treating plant according to claim 1 is characterized in that: be provided with transfusion force (forcing) pump (8) between said gas absorption jar (7) and the said high-density cleaner (9).
3. a kind of rubbish cracking treating plant according to claim 2 is characterized in that: be provided with one-level accurate filter (12) between said blower fan (11) and the said gas sweetening adsorption tower (13).
4. a kind of rubbish cracking treating plant according to claim 3 is characterized in that: the clean gas drain place of said gas sweetening adsorption tower (13) is provided with secondary accurate filter (14).
5. according to claim 1 or 2 or 3 described a kind of rubbish cracking treating plants, it is characterized in that: the said e Foerderanlage that feeds intake comprises rubbish collection bucket (22) and travelling belt (23).
6. according to claim 1 or 2 or 3 described a kind of rubbish cracking treating plants, it is characterized in that: said housing (21) outside also is equipped with work staircase (24).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204688031U CN202359072U (en) | 2011-11-23 | 2011-11-23 | Refuse cracking-purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204688031U CN202359072U (en) | 2011-11-23 | 2011-11-23 | Refuse cracking-purifying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202359072U true CN202359072U (en) | 2012-08-01 |
Family
ID=46570275
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204688031U Expired - Lifetime CN202359072U (en) | 2011-11-23 | 2011-11-23 | Refuse cracking-purifying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202359072U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102433139A (en) * | 2011-11-23 | 2012-05-02 | 珠海新市节能环保科技有限公司 | Garbage cracking purification device and garbage cracking purification treatment process |
| CN103700302A (en) * | 2013-12-02 | 2014-04-02 | 同济大学 | Waste pyrolysis integrated experimental apparatus for teaching experiment |
-
2011
- 2011-11-23 CN CN2011204688031U patent/CN202359072U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102433139A (en) * | 2011-11-23 | 2012-05-02 | 珠海新市节能环保科技有限公司 | Garbage cracking purification device and garbage cracking purification treatment process |
| CN103700302A (en) * | 2013-12-02 | 2014-04-02 | 同济大学 | Waste pyrolysis integrated experimental apparatus for teaching experiment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102433139B (en) | Garbage cracking purification device and garbage cracking purification treatment process | |
| CN201659136U (en) | Domestic garbage and organic waste gasifying-liquefying treatment system | |
| CN202356390U (en) | Renewable energy source and resource utilization system in living garbage disposal site | |
| CN103599916B (en) | A kind of Non-oxygen pyrolytic process is died of illness the method and apparatus of domestic animal and organic garbage of city | |
| CN2926833Y (en) | System and apparatus for firing medical refuse | |
| CN208066104U (en) | A kind of chemical industry waste water station foul smell is collected and processing system | |
| CN207271789U (en) | A kind of oil-containing solid waste microwave thermal desorbs recycling treatment system | |
| CN202359072U (en) | Refuse cracking-purifying equipment | |
| CN205613263U (en) | Reation kettle tail gas processing apparatus | |
| CN202028603U (en) | High temperature and high pressure medical solid waste on-site disposing device | |
| CN104056530A (en) | Contaminated soil thermal decomposition tail gas treatment method | |
| CN102125926B (en) | High temperature and high pressure on-site treating device for medical solid wastes | |
| KR101334880B1 (en) | Waste disposal system and exhaust gas to prevent the device used in the system | |
| CN109925869A (en) | Flue gas of refuse burning high-efficient purification processing method | |
| CN213599378U (en) | Domestic refuse incineration treatment equipment | |
| CN206121518U (en) | Novel waste gas treating system | |
| CN202045124U (en) | Plasma medical solid waste in-situ disposal device | |
| CN205115378U (en) | City domestic waste dry distillation system | |
| CN201625658U (en) | Organic waste cracking and carbonizing system with novel tail gas treating device | |
| CN108211626A (en) | Exhaust gas purification system and purification method after a kind of domestic garbage pyrolysis gasification | |
| CN209857072U (en) | Mobile high-temperature anaerobic incineration/cracking device for household garbage | |
| CN210814727U (en) | Distributed household garbage low-temperature reduction harmless system | |
| CN102189095B (en) | Plasma medical solid waste on-site treatment device | |
| CN203408625U (en) | Organic waste gas treatment equipment | |
| CN207990630U (en) | A kind of hospital refuse processor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HU YUN Free format text: FORMER OWNER: ZHUHAI XINSHI ENERGY SAVING ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Effective date: 20130620 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20130620 Address after: 519000 No. 82 Shannon Road, Guangdong, Zhuhai Patentee after: Hu Yun Address before: 519000 No. 82 Shannon Road, Guangdong, Zhuhai Patentee before: Zhuhai Xinshi Energy-Saving Environmental Protection Technology Co., Ltd. |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20120801 Effective date of abandoning: 20140122 |
|
| RGAV | Abandon patent right to avoid regrant |