CN113787083A - Garbage recycling treatment process - Google Patents
Garbage recycling treatment process Download PDFInfo
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- CN113787083A CN113787083A CN202111110462.5A CN202111110462A CN113787083A CN 113787083 A CN113787083 A CN 113787083A CN 202111110462 A CN202111110462 A CN 202111110462A CN 113787083 A CN113787083 A CN 113787083A
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- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 125
- 238000000034 method Methods 0.000 title claims abstract description 36
- 230000008569 process Effects 0.000 title claims abstract description 34
- 238000004064 recycling Methods 0.000 title claims abstract description 18
- 239000000654 additive Substances 0.000 claims abstract description 36
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims abstract description 36
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 35
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims abstract description 22
- 238000006731 degradation reaction Methods 0.000 claims abstract description 16
- 239000003109 Disodium ethylene diamine tetraacetate Substances 0.000 claims abstract description 14
- ZGTMUACCHSMWAC-UHFFFAOYSA-L EDTA disodium salt (anhydrous) Chemical compound [Na+].[Na+].OC(=O)CN(CC([O-])=O)CCN(CC(O)=O)CC([O-])=O ZGTMUACCHSMWAC-UHFFFAOYSA-L 0.000 claims abstract description 14
- 235000019301 disodium ethylene diamine tetraacetate Nutrition 0.000 claims abstract description 14
- 150000004659 dithiocarbamates Chemical class 0.000 claims abstract description 14
- UEUXEKPTXMALOB-UHFFFAOYSA-J tetrasodium;2-[2-[bis(carboxylatomethyl)amino]ethyl-(carboxylatomethyl)amino]acetate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]C(=O)CN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O UEUXEKPTXMALOB-UHFFFAOYSA-J 0.000 claims abstract description 14
- 239000000126 substance Substances 0.000 claims abstract description 13
- 230000015556 catabolic process Effects 0.000 claims abstract description 11
- 239000002245 particle Substances 0.000 claims abstract description 11
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 230000000844 anti-bacterial effect Effects 0.000 claims abstract description 8
- 239000003899 bactericide agent Substances 0.000 claims abstract description 8
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 8
- 238000005303 weighing Methods 0.000 claims abstract description 4
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N dimethyl sulfoxide Natural products CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 18
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 claims description 17
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 17
- 239000000600 sorbitol Substances 0.000 claims description 17
- 238000011084 recovery Methods 0.000 claims description 8
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 5
- 230000000996 additive effect Effects 0.000 claims description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 5
- 239000002699 waste material Substances 0.000 claims description 5
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical group CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 claims description 4
- 239000012991 xanthate Substances 0.000 claims description 4
- IAZDPXIOMUYVGZ-WFGJKAKNSA-N Dimethyl sulfoxide Chemical group [2H]C([2H])([2H])S(=O)C([2H])([2H])[2H] IAZDPXIOMUYVGZ-WFGJKAKNSA-N 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 239000002516 radical scavenger Substances 0.000 claims description 2
- 230000003115 biocidal effect Effects 0.000 claims 1
- 239000003139 biocide Substances 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 9
- 150000002500 ions Chemical class 0.000 description 9
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- 229920003023 plastic Polymers 0.000 description 7
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- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 5
- 229920002125 Sokalan® Polymers 0.000 description 5
- 229960001631 carbomer Drugs 0.000 description 5
- 230000000855 fungicidal effect Effects 0.000 description 5
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- 241000894006 Bacteria Species 0.000 description 4
- 239000004519 grease Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000004566 building material Substances 0.000 description 3
- 239000004568 cement Substances 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000011152 fibreglass Substances 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
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- 239000006260 foam Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
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- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000004599 antimicrobial Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
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- 238000003912 environmental pollution Methods 0.000 description 1
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- 210000003608 fece Anatomy 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical class FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 235000012055 fruits and vegetables Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
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- 239000002440 industrial waste Substances 0.000 description 1
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- 238000005342 ion exchange Methods 0.000 description 1
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- JPMIIZHYYWMHDT-UHFFFAOYSA-N octhilinone Chemical compound CCCCCCCCN1SC=CC1=O JPMIIZHYYWMHDT-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000012667 polymer degradation Methods 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
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- 230000000644 propagated effect Effects 0.000 description 1
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- 230000009467 reduction Effects 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention provides a garbage recycling treatment process, and relates to the technical field of garbage treatment. A garbage recycling treatment process comprises the following steps: treating the garbage at the temperature of 105-150 ℃ for 10-15min, and crushing the garbage until the particle size is below 18 mm; weighing the following additives according to the weight percentage of the garbage: 0.03-0.11% of diethylene glycol, 0.01-0.05% of disodium ethylene diamine tetraacetate, 0.01-0.08% of tetrasodium ethylene diamine tetraacetate, 0.02-0.13% of heavy metal trapping agent, 0.02-0.18% of dithiocarbamate derivative, 0.01-0.03% of barium sulfate, 0.01-0.06% of medium carbon alcohol substance, 0.01-0.03% of degradation promoter and 0.005-0.015% of bactericide; and the additives are thrown into the garbage which is being crushed in turn. The present invention can perform harmless treatment of garbage by this operation.
Description
Technical Field
The invention relates to the technical field of garbage treatment, in particular to a garbage recycling treatment process.
Background
Along with the rapid development of the socioeconomic rapid progress of China and the rapid improvement of the living standard of people, the garbage generated in the urban production and living process is rapidly increased, and the domestic garbage occupies land, pollutes the environment and has more obvious influence on the health of people. Specifically, the waste has caused a great hazard: organic matters are rotten, compounds are decomposed, ammonia, hydrogen sulfide, odor and other toxic and harmful gases are emitted, and the atmosphere is polluted; viruses, flora, ova and the like are propagated, bred and spread; pollutants permeate into the stratum along with sewage and flow into a river channel to pollute the land and an underground water system; the metals and their compounds are resolved or ionized, and pollute water and land. The garbage is classified into industrial waste garbage, mining waste garbage, municipal waste garbage, agricultural waste garbage, radioactive waste garbage and the like according to the source. Wherein the municipal solid waste is also called municipal refuse; the production amount of organic solid waste garbage such as organic components, fruit and vegetable garbage, livestock and poultry manure, straw and the like in urban garbage of urban residents is continuously increased, the proportion of the garbage in the household garbage is high, and huge pressure is brought to the collection, transportation and treatment of the current urban household garbage.
The great increase of garbage makes the garbage treatment more and more difficult, and the problems of environmental pollution and the like caused by the increase of garbage gradually attract the wide attention of all social circles. In China, to realize the industrialization, resource utilization, reduction and harmlessness of garbage, mixed collection, low content and heat value of recyclable materials, and high water content and biodegradable organic content of the garbage must be faced. In response to these problems, various techniques are also applied.
The first is incineration, the traditional garbage treatment generally adopts incineration or crushing recycling, the incineration method directly carries out unified incineration treatment on the garbage, the incineration has the advantages that the generated heat energy can generate electricity and heat, the treatment speed is high, the defects are that a plurality of toxic and harmful substances can be generated, such as rubber plastics or waste oil and other high molecular organic compounds can generate a large amount of toxic gases in the incineration process, such as toluene, fluorocarbon derivatives, dioxin, sulfur dioxide and the like, and the pollution is caused to the atmosphere, water, soil and plants.
The second is deep burying, and the advantage of deep burying is convenient economy, can compress the rubbish shaping, buries underground at a certain degree of depth, and although the foundation ditch has taken waterproof impervious isolation measure, many high molecular polymer degradation need very long time, still can wrap up and hold many bacterial virus in the deep burying process.
The third is to make compost, but may cause the transfer and diffusion of pollutants, especially heavy metal pollutants, to directly pollute farmlands and plants.
If the garbage can be recycled, the garbage disposal problem can be solved on one hand, and on the other hand, resources can be fully utilized.
Disclosure of Invention
The invention aims to provide a garbage recycling treatment process, which has the advantages of fully and effectively utilizing garbage and solving the problem of garbage treatment.
The technical problem to be solved by the invention is realized by adopting the following technical scheme.
The embodiment of the application provides a garbage recycling treatment process, which comprises the following steps:
treating the garbage at the temperature of 105-150 ℃ for 10-15min, and crushing the garbage until the particle size is below 18 mm;
weighing the following additives according to the weight percentage of the garbage: 0.03-0.11% of diethylene glycol, 0.01-0.05% of disodium ethylene diamine tetraacetate, 0.01-0.08% of tetrasodium ethylene diamine tetraacetate, 0.02-0.13% of heavy metal trapping agent, 0.02-0.18% of dithiocarbamate derivative, 0.01-0.03% of barium sulfate, 0.01-0.06% of medium carbon alcohol substance, 0.01-0.03% of degradation promoter and 0.005-0.015% of bactericide; and the additives are thrown into the garbage which is being crushed in turn.
Compared with the prior art, the embodiment of the invention has at least the following advantages or beneficial effects:
through the operation, the garbage can be harmlessly treated, and the prepared granular substances can replace sand, wood dust and foam, can be stirred with cement, can be used as building materials, and can also be used for producing living products, such as glass fiber reinforced plastics, partition boards and heat-insulating materials. According to the invention, the surface area of the garbage is increased by crushing the garbage, so that the garbage can be conveniently reacted with the additive in the subsequent process, and the garbage can be decomposed and treated better; the disodium ethylene diamine tetraacetate and tetrasodium ethylene diamine tetraacetate can perform a displacement reaction with heavy metal ions to generate a complex, so that a heavy metal trapping agent can conveniently react with the complex to generate a precipitate; the heavy metal trapping agent is added to react with heavy metal ions in the garbage and form a flocculation state in a short time, so that heavy metal substances are trapped and separated; by adding the dithiocarbamate derivative, the garbage reaction can be promoted, the heavy metal capture time is shortened, and the reaction process is accelerated; the degradation accelerator is added to promote the garbage degradation reaction and accelerate the garbage recovery treatment process; the bactericide is added, so that bacteria can be killed, and the quality of the treated garbage is ensured; by adding the diglycol, resin and grease in the garbage can be dissolved, plastics can be degraded, and heavy metals can be complexed to play a role in fixing the heavy metals; in addition, the treatment at high temperature can accelerate the plastic reaction and the garbage recovery treatment speed.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below. The examples, in which specific conditions are not specified, were conducted under conventional conditions or conditions recommended by the manufacturer. The reagents or instruments used are not indicated by the manufacturer, and are all conventional products available commercially.
It should be noted that the embodiments and features of the embodiments in the present application may be combined with each other without conflict. The present invention will be described in detail below with reference to specific examples.
The features and properties of the present invention are described in further detail below with reference to examples.
The invention provides a garbage recycling treatment process, which comprises the following steps: treating the garbage at the temperature of 105-150 ℃ for 10-15min, and crushing the garbage until the particle size is below 18 mm; weighing the following additives according to the weight percentage of the garbage: 0.03-0.11% of diethylene glycol, 0.01-0.05% of disodium ethylene diamine tetraacetate, 0.01-0.08% of tetrasodium ethylene diamine tetraacetate, 0.02-0.13% of heavy metal trapping agent, 0.02-0.18% of dithiocarbamate derivative, 0.01-0.03% of barium sulfate, 0.01-0.06% of medium carbon alcohol substance, 0.01-0.03% of degradation promoter and 0.005-0.015% of bactericide; and the additives are thrown into the garbage which is being crushed in turn. Through the operation, the garbage can be harmlessly treated, and the prepared granular substances can replace sand, wood dust and foam, can be stirred with cement, can be used as building materials, and can also be used for producing living products, such as glass fiber reinforced plastics, partition boards and heat-insulating materials. According to the invention, the surface area of the garbage is increased by crushing the garbage, so that the garbage can be conveniently reacted with the additive in the subsequent process, and the garbage can be decomposed and treated better; the disodium ethylene diamine tetraacetate and tetrasodium ethylene diamine tetraacetate can perform a displacement reaction with heavy metal ions to generate a complex, so that a heavy metal trapping agent can conveniently react with the complex to generate a precipitate; the heavy metal trapping agent is added to react with heavy metal ions in the garbage and form a flocculation state in a short time, so that heavy metal substances are trapped and separated; by adding the dithiocarbamate derivative, the garbage reaction can be promoted, the heavy metal capture time is shortened, and the reaction process is accelerated; the degradation accelerator is added to promote the garbage degradation reaction and accelerate the garbage recovery treatment process; the bactericide is added, so that bacteria can be killed, and the quality of the treated garbage is ensured; by adding the diglycol, resin and grease in the garbage can be dissolved, plastics can be degraded, and heavy metals can be complexed to play a role in fixing the heavy metals; in addition, the treatment at high temperature can accelerate the plastic reaction and the garbage recovery treatment speed.
In some embodiments of the present invention, the heavy metal scavenger is a xanthate. The xanthate substance can be subjected to bonded ion exchange transfer with heavy metal particles, so that the heavy metal ions are separated out, and then the heavy metal ions are precipitated and separated out.
In some embodiments of the present invention, the number of carbon atoms of the medium carbon alcohol is 6-18.
In some embodiments of the present invention, the medium carbon alcohol is sorbitol. Can adsorb grease and capture heavy metal ions.
In some embodiments of the invention, the sorbitol concentration is 15-25%. At this concentration, the treatment efficiency is high.
In some embodiments of the present invention, the degradation promoter is dimethyl sulfoxide, ammonia water, or N, N-Dimethylformamide (DMF). Dimethyl sulfoxide has high selective extraction capacity, can effectively promote the garbage degradation reaction and accelerate the garbage recovery and treatment process; ammonia water or N, N-Dimethylformamide (DMF) also has the advantage of promoting the garbage degradation reaction.
In some embodiments of the present invention, the concentration of dimethyl sulfoxide is 10-20%.
In some embodiments of the invention, the antimicrobial agent is a cason. The kasong has good sterilization performance, can kill bacteria in garbage, and ensures the garbage treatment effect.
In some embodiments of the present invention, the above additives are added at intervals of 1-3 min.
In some embodiments of the present invention, the above-mentioned crushing rate is 900-1100r/min, and the crushing is continued for 1-3min after each additive is added.
Example 1
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 105 ℃ for 10min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.03% of diethylene glycol, 0.01% of disodium ethylenediaminetetraacetate, 0.01% of tetrasodium ethylenediaminetetraacetate, 0.02% of sorbitol (concentration of 15%), 0.02% of dithiocarbamate derivatives, 0.01% of barium sulfate, 0.01% of sorbitol, 0.01% of dimethyl sulfoxide and 0.005% of a carbomer fungicide; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing speed is 900r/min, and the crushing is continued for 1min after the additives are added.
Example 2
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 115 ℃ for 12min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.06% of diethylene glycol, 0.02% of disodium ethylenediaminetetraacetate, 0.03% of tetrasodium ethylenediaminetetraacetate, 0.06% of xanthate substances, 0.07% of dithiocarbamate derivatives, 02% of barium sulfate, 0.02% of sorbitol (concentration of 18%), 0.02% of dimethyl sulfoxide and 0.008% of a Kathon fungicide; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing speed is 1500r/min, and the crushing is continued for 2min after the additives are added.
Example 3
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 125 ℃ for 13min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.08% of diethylene glycol, 0.03% of disodium ethylenediaminetetraacetate, 0.04% of tetrasodium ethylenediaminetetraacetate, 0.1% of sorbitol (concentration of 21%), 0.13% of dithiocarbamate derivatives, 0.02% of barium sulfate, 0.03% of sorbitol, 0.02% of dimethyl sulfoxide and 0.01% of a carbomer fungicide; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing speed is 2000r/min, and the crushing is continued for 2min after the additives are added.
Example 4
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 135 ℃ for 13min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.1% diethylene glycol, 0.04% disodium ethylenediaminetetraacetate, 0.06% tetrasodium ethylenediaminetetraacetate, 0.11% sorbitol (concentration of 24%), 0.15% dithiocarbamate derivatives, 0.03% barium sulfate, 0.04% sorbitol, 0.03% dimethyl sulfoxide, and 0.013% carbomer; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing speed is 2500r/min, and the crushing is continued for 2min after the additives are added.
Example 5
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 150 ℃ for 13min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.11% of diethylene glycol, 0.05% of disodium ethylenediaminetetraacetate, 0.08% of tetrasodium ethylenediaminetetraacetate, 0.13% of sorbitol (concentration of 25%), 0.18% of dithiocarbamate derivatives, 0.03% of barium sulfate, 0.06% of sorbitol, 0.03% of dimethyl sulfoxide and 0.015% of a carbomer fungicide; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing rate is 2800r/min, and the crushing is continued for 3min after the additives are added.
Example 6
This example differs from example 3 in that: the degradation promoter is ammonia water.
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 125 ℃ for 13min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.08% of diethylene glycol, 0.03% of disodium ethylenediaminetetraacetate, 0.04% of tetrasodium ethylenediaminetetraacetate, 0.1% of sorbitol (concentration of 21%), 0.13% of dithiocarbamate derivatives, 0.02% of barium sulfate, 0.03% of sorbitol, 0.02% of ammonia water and 0.01% of a carbomer fungicide; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing speed is 2000r/min, and the crushing is continued for 2min after the additives are added.
Example 7
This example differs from example 3 in that: the degradation accelerator is N, N-dimethylformamide.
A garbage recycling treatment process comprises the following steps:
treating 100kg of garbage at 125 ℃ for 13min, and crushing until the particle size is below 18 mm;
taking the following additives according to the weight percentage of the garbage: 0.08% of diethylene glycol, 0.03% of disodium ethylenediaminetetraacetate, 0.04% of tetrasodium ethylenediaminetetraacetate, 0.1% of sorbitol (concentration of 21%), 0.13% of dithiocarbamate derivatives, 0.02% of barium sulfate, 0.03% of sorbitol, 0.02% of N, N-dimethylformamide and 0.01% of a KASON bactericide; and the additives are put into the garbage which is being crushed in turn;
wherein the crushing speed is 2000r/min, and the crushing is continued for 2min after the additives are added.
In conclusion, the invention can treat garbage harmlessly by the operation, and the prepared granular substance can replace sand, wood dust and foam, can be stirred with cement, can be used as building materials, and can also be used for producing living products, such as glass fiber reinforced plastics, partition boards and heat insulation materials. According to the invention, the surface area of the garbage is increased by crushing the garbage, so that the garbage can be conveniently reacted with the additive in the subsequent process, and the garbage can be decomposed and treated better; the disodium ethylene diamine tetraacetate and tetrasodium ethylene diamine tetraacetate can perform a displacement reaction with heavy metal ions to generate a complex, so that a heavy metal trapping agent can conveniently react with the complex to generate a precipitate; the heavy metal trapping agent is added to react with heavy metal ions in the garbage and form a flocculation state in a short time, so that heavy metal substances are trapped and separated; by adding the dithiocarbamate derivative, the garbage reaction can be promoted, the heavy metal capture time is shortened, and the reaction process is accelerated; the degradation accelerator is added to promote the garbage degradation reaction and accelerate the garbage recovery treatment process; the bactericide is added, so that bacteria can be killed, and the quality of the treated garbage is ensured; by adding the diglycol, resin and grease in the garbage can be dissolved, plastics can be degraded, and heavy metals can be complexed to play a role in fixing the heavy metals; in addition, the treatment at high temperature can accelerate the plastic reaction, thereby accelerating the garbage recovery treatment speed.
The embodiments described above are some, but not all embodiments of the invention. The detailed description of the embodiments of the present invention is not intended to limit the scope of the invention as claimed, but is merely representative of selected embodiments of the invention. 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.
Claims (10)
1. A garbage recycling treatment process is characterized by comprising the following steps:
treating the garbage at the temperature of 105-150 ℃ for 10-15min, and crushing the garbage until the particle size is below 18 mm;
weighing the following additives according to the weight percentage of the garbage: 0.03-0.11% of diethylene glycol, 0.01-0.05% of disodium ethylene diamine tetraacetate, 0.01-0.08% of tetrasodium ethylene diamine tetraacetate, 0.02-0.13% of heavy metal trapping agent, 0.02-0.18% of dithiocarbamate derivative, 0.01-0.03% of barium sulfate, 0.01-0.06% of medium carbon alcohol substance, 0.01-0.03% of degradation promoter and 0.005-0.015% of bactericide; and the additives are thrown into the garbage which is being crushed in turn.
2. The process of claim 1, wherein the heavy metal scavenger is a xanthate.
3. The process according to claim 1, wherein the number of carbon atoms in the medium carbon alcohol is 6 to 18.
4. The process of claim 3, wherein the medium carbon alcohol is sorbitol.
5. The process of claim 4, wherein the sorbitol concentration is 15-25%.
6. The process of claim 1, wherein the degradation promoter is dimethyl sulfoxide, ammonia water or N, N-dimethylformamide.
7. The process of claim 6, wherein the concentration of dimethyl sulfoxide is 10-20%.
8. A waste recovery process according to claim 1, wherein the biocide is cason.
9. The garbage recycling process of claim 1, wherein the input time interval of each additive is 1-3 min.
10. The process as claimed in claim 1, wherein the crushing rate is 900-2800r/min, and the crushing is continued for 1-3min after the additives are added.
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006007186A (en) * | 2004-06-29 | 2006-01-12 | Jfe Steel Kk | Scavenger for heavy metals and separation/removal method for heavy metals |
CN1934177A (en) * | 2004-03-26 | 2007-03-21 | 松下电工株式会社 | Method of decomposing plastic |
CN102240661A (en) * | 2011-05-16 | 2011-11-16 | 云南天远生态环保科技有限责任公司 | Pretreatment method and equipment for household garbage |
CN202933926U (en) * | 2012-06-01 | 2013-05-15 | 浩蓝环保股份有限公司 | Apparatus used for restoration and treatment of heavy metal pollutions in mining area |
CN103721997A (en) * | 2013-12-10 | 2014-04-16 | 湖南省同力电子废弃物回收拆解利用有限公司 | Three wastes systemic treatment technology and process for electronic waste recovery and treatment |
CN104556332A (en) * | 2014-12-25 | 2015-04-29 | 上海源育节能环保科技有限公司 | Heavy metal ion trapping agent and manufacturing method thereof |
CN106315808A (en) * | 2016-10-13 | 2017-01-11 | 仲恺农业工程学院 | Heavy metal chelating agent and preparation method thereof |
-
2021
- 2021-09-18 CN CN202111110462.5A patent/CN113787083A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1934177A (en) * | 2004-03-26 | 2007-03-21 | 松下电工株式会社 | Method of decomposing plastic |
JP2006007186A (en) * | 2004-06-29 | 2006-01-12 | Jfe Steel Kk | Scavenger for heavy metals and separation/removal method for heavy metals |
CN102240661A (en) * | 2011-05-16 | 2011-11-16 | 云南天远生态环保科技有限责任公司 | Pretreatment method and equipment for household garbage |
CN202933926U (en) * | 2012-06-01 | 2013-05-15 | 浩蓝环保股份有限公司 | Apparatus used for restoration and treatment of heavy metal pollutions in mining area |
CN103721997A (en) * | 2013-12-10 | 2014-04-16 | 湖南省同力电子废弃物回收拆解利用有限公司 | Three wastes systemic treatment technology and process for electronic waste recovery and treatment |
CN104556332A (en) * | 2014-12-25 | 2015-04-29 | 上海源育节能环保科技有限公司 | Heavy metal ion trapping agent and manufacturing method thereof |
CN106315808A (en) * | 2016-10-13 | 2017-01-11 | 仲恺农业工程学院 | Heavy metal chelating agent and preparation method thereof |
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