CN115287108A - Regenerated clean fuel produced by using oily sludge and manufacturing method thereof - Google Patents

Regenerated clean fuel produced by using oily sludge and manufacturing method thereof Download PDF

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CN115287108A
CN115287108A CN202210818694.4A CN202210818694A CN115287108A CN 115287108 A CN115287108 A CN 115287108A CN 202210818694 A CN202210818694 A CN 202210818694A CN 115287108 A CN115287108 A CN 115287108A
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fermentation
sludge
oily sludge
temperature
powder
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李佳
李健
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/46Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/06Treatment of sludge; Devices therefor by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/14Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
    • C02F11/148Combined use of inorganic and organic substances, being added in the same treatment step
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • C10L5/442Wood or forestry waste
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/48Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/02Odour removal or prevention of malodour
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/08Drying or removing water
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/26Composting, fermenting or anaerobic digestion fuel components or materials from which fuels are prepared
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Ecology (AREA)
  • Forests & Forestry (AREA)
  • Wood Science & Technology (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Treatment Of Sludge (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention relates to a regenerated clean fuel produced by using oily sludge and a manufacturing method thereof, wherein the oily sludge with the water content of 80 percent, fly ash, forestry wastes, quick lime, ferrous sulfate, magnesium sulfate, polyacrylamide and chlorine dioxide are uniformly mixed, high-temperature rapid fermentation is adopted, the temperature of a fermentation machine is raised to 100 ℃ through oil-electricity heat conduction and is kept for 2 hours, the temperature is kept at 60-80 ℃, high-temperature resistant active strains are added for fermentation, a stirring system of the fermentation machine is adjusted to an intermittent stirring function, the fermentation time of the oily sludge in the fermentation machine is 10 hours, and fermented clinker is aged, cooled, crushed and screened to prepare mixed powder with the particle size of less than 0.02 mm; and then the uniformly mixed powder is conveyed to a special storage silo, and is packaged by a full-automatic electronic metering weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product.

Description

Regenerated clean fuel produced by oil-containing sludge and manufacturing method thereof
Technical Field
The invention relates to a regenerated clean fuel produced by oil-containing sludge and a manufacturing method thereof, in particular to oil-containing sludge derivative powder prepared by mechanically and fully automatically performing high-temperature rapid fermentation, disinfection and sterilization, drying, crushing and screening on oil-containing sludge, fly ash and forestry waste, which is used as a combustion raw material of a coal-fired power plant and belongs to the field of waste treatment.
Background
The oily sludge is the combination of active sludge generated after the industrial wastewater of an oil refinery, electroplating wastewater, oily wastewater and domestic sewage are treated by methods of flotation, filtration, flocculation, chemistry, physics and the like, crude oil separation tank bottom sludge, flotation tank scum, oily sludge of crude oil tank bottom sludge and the like, the components of the sludge are complex, the oil-containing sludge generally has an oil content of 10-30% and a water content of 50-90%, in the petrochemical industry of China, more than 200 million tons of tank bottom sludge and tank bottom sludge are generated each year on average, the components of the sludge are complex, the sludge contains a large amount of aged crude oil, wax, asphaltene, colloid and solid suspended matters, bacteria, salts, acid gas and corrosion products, a large amount of sewage treatment agents such as coagulator, flocculant, corrosion inhibitor, scale inhibitor, bactericide and the like are added in the sewage treatment process, and substances such as benzene series, phenols, anthracene and the like are contained, and the odor and toxicity are accompanied by oil in water (O/W), water-in-oil (W/O) and suspended solids; suspended solids and colloidal particles in the oily sludge form a very stable emulsification system with oil and water, the viscosity is high, the sedimentation is difficult, the oily sludge is large in volume and various in types, and the emulsification system comprises: waste drilling mud generated in the process of petroleum exploitation, oil-water and hydrocarbon-water mixture generated in the process of cleaning mineral oil storage and transportation facilities, oily sludge generated in the processes of storage facilities, oil-water solid matter separators, water accumulation tanks, ditches and other transportation pipelines, sewage pools and rainwater collection pipelines in the primary petroleum refining process, oily sludge generated in oil separation tanks in the petroleum refining process, sludge generated in the treatment processes of gasoline refining process wastewater and cooling wastewater, scum generated in the dissolved gas flotation process in the petroleum refining process, overflowing waste oil or emulsion generated in the petroleum refining process, oily sludge generated in the cleaning process of petroleum refining heat exchanger tube bundles, settled bottom sediment of oil slurry tanks in the petroleum refining process, residue generated by an oil inlet pipeline filtering or separating device in the petroleum refining process, and waste filtering medium generated in the petroleum refining process, waste mineral oil and oil sludge produced in the centralized disassembly process of internal combustion engines, automobiles and ships, waste mineral oil and oil sludge produced in the honing, grinding and polishing processes, waste kerosene, diesel oil, gasoline and other solvent oil produced by refining petroleum and kerosene produced in the process of cleaning metal parts, waste mineral oil produced by using quenching oil to carry out surface hardening treatment, waste mineral oil produced by using rolling oil, a coolant and acid to carry out metal rolling, waste mineral oil produced by tinning and recycling processes, waste oil, oil sludge and scum produced by waste water treatment produced by oil-water separation facilities, waste solvent oil produced in the rubber production process, precipitation residue, filtering residue and waste filtering adsorption medium produced in the regeneration and purification process of waste mineral oil, cracking residue produced in the cracking and regeneration process of waste mineral oil, and oil sludge produced in the storage process of waste fuel oil and oil, floating oil and sludge generated in the air flotation, oil removal and flocculation precipitation treatment processes of the petroleum refining wastewater; if the soil is not treated and directly buried, not only a large amount of cultivated land is occupied, but also the surrounding soil, water and air can cause environmental pollution; and harmful components such as heavy metals; copper, chromium, arsenic, mercury, cadmium, lead, nickel, zinc and the like, pathogenic bacteria, parasitic ova, organic pollutants and odor become a great public nuisance which affects the urban environmental sanitation, governments at all levels and related departments actively seek effective treatment technologies, and the treatment method of oily sludge in China at present mainly adopts a landfill method to treat so as to reduce the pollution to the environment; how to properly and scientifically treat the oily sludge to achieve reduction, stabilization, harmlessness and reclamation becomes a large research topic which is widely concerned by scientific and technical personnel in China and even the world environment.
Disclosure of Invention
The invention aims to solve the problems and provide the clean fuel for recycling the oily sludge produced by using the oily sludge, the fly ash and the forestry waste as the raw materials, thereby solving the problem of environmental pollution caused by the oily sludge, the fly ash and the forestry waste, also solving the problem of recycling the oily sludge and the fly ash, changing waste into valuable and benefiting chemical hazard, and realizing the virtuous cyclic utilization of the solid waste resources. The method is characterized in that mechanized full-automatic high-temperature rapid fermentation is adopted, and the oily sludge is sterilized, so that the oily sludge with the water content of 80 percent is changed into organic matter regenerated powder fuel within 12 hours and can be used as a combustion raw material of a coal-fired power plant; realizes the resource comprehensive utilization of the oily sludge and thoroughly solves the problem of pollution of the oily sludge to the ecological environment.
In order to achieve the aim, the invention provides a regenerated clean fuel produced by using oily sludge, which is prepared from the following raw materials in parts by weight:
Figure RE-GDA0003832416250000031
the oily sludge is the combination of activated sludge generated by the industrial wastewater of an oil refinery, electroplating wastewater, oily wastewater and domestic sewage generated in the petroleum mechanical processing process and the oily sludge of the bottom sludge of a crude oil separation tank, floating slag of a flotation tank and the bottom sludge of a crude oil tank after the activated sludge is treated by flotation, filtration, flocculation and chemical methods;
the fly ash powder is a volcanic ash-like mixed material formed by high-temperature combustion of coal powder; coal is ground into coal powder with the particle size of less than 100 microns by a thermal power plant, preheated air is sprayed into a hearth to be combusted in a suspension state, high-temperature flue gas mixed with a large amount of non-combustible substances is generated, and the coal powder is collected by a dust collecting device to obtain fly ash; magnetic separation, drying and screening are carried out to prepare powder with the particle size of less than 0.02 mm;
the forestry waste powder refers to forestry felling residues, wood making residues and processing residues, and comprises branches, treetops, barks, leaves, roots and rattans, shrubs, wood making truncated ends, slabs, laths, wood bamboo truncated ends, sawdust, crushed veneers, wood cores, wood shavings, wood blocks, thin bamboo veneers, leftover bits and waste residues, and the powder with the particle size of less than 5mm is prepared after crushing, sorting, magnetic separation, drying, crushing, grinding and screening;
the quick lime powder is prepared by calcining limestone at high temperature, crushing, sorting, crushing, grinding and screening to obtain powder with the particle size of less than 0.02 mm;
the polyacrylamide is white powder or small particles, and the density is 1.32g/cm 3
In order to achieve the aim, the invention also discloses a method for manufacturing the regenerated clean fuel produced by the oily sludge, which comprises the following steps: mixing and stirring oil-containing sludge with water content of 80%, fly ash powder, forestry waste powder, quicklime powder, ferrous sulfate, magnesium sulfate, polyacrylamide and chlorine dioxide uniformly according to the proportion, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8;
conveying the sludge into a sealed high-temperature fermentation machine by adopting a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding a special sludge fermentation strain and a thermophilic high-temperature resistant active bacteria composite flora agent in proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of the thermophilic high-temperature resistant composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by utilizing the activity function of the thermophilic high-temperature resistant composite flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, and the method is used for killing harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge;
the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved;
the fermented oily sludge clinker is cooled, crushed and sieved to prepare mixed powder with the particle size of less than 0.02mm, and the mixed powder is conveyed to a special storage silo.
Optionally, the fermentation of the oily sludge adopts a mechanical full-automatic high-temperature sealed fermentation device, the high temperature in the device is based on the principle of heating oil by electricity, and an oil-separating layer is arranged in the device and a fermentation method of heating by oil-electricity heat conduction is adopted.
Optionally, the fermentation strain of the oily sludge comprises a sludge special fermentation strain and a thermophilic high-temperature resistant active bacteria composite microbial agent which are mixed in proportion.
Optionally, the mixing and stirring of the oily sludge is carried out by uniformly mixing and stirring by using a double-shaft humidifying mixing stirrer.
Optionally, a full-automatic electronic metering weighing packaging machine system is adopted to package the powder material conveyed to the special storage silo.
Optionally, the method comprises:
taking 65-75 parts by weight of oily sludge with water content of 80%, 25-35 parts by weight of fly ash powder, 25-30 parts by weight of forestry waste powder, 13-18 parts by weight of quick lime powder, 8-13 parts by weight of ferrous sulfate, 13-18 parts by weight of magnesium sulfate, 0.3-0.6 part by weight of polyacrylamide and 0.3-0.6 part by weight of chlorine dioxide, and uniformly mixing and stirring by adopting a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the mixture into a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ by using oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.01-0.05 weight part of sludge special fermentation strain and 0.02-0.06 weight part of thermophilic high-temperature resistant active bacteria composite microbial flora agent according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic high-temperature resistant bacteria composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by using the activity function of the thermophilic high-temperature resistant composite microbial flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, and the method is used for killing harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; the fermented oily sludge clinker is cooled, crushed and screened to prepare mixed powder with the particle size of less than 0.02mm, the mixed powder is conveyed to a special storage silo and is packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, aged and harmless organic matter clean fuel product.
The invention mainly aims to overcome the defect that the existing technology (landfill, incineration, burning and curing) is used for treating the oily sludge, and aims at the national regulation on treatment of dangerous solid wastes and urban sludge, a new technology for quickly treating the oily sludge with the water content of 80% at high temperature is researched; a flora agent prepared by mixing, domesticating, culturing and reactivating a plurality of high-quality microbial strains and ferment is used as a rapid leavening agent of oily sludge with the water content of 80 percent, and the microbial strain agent is an activating microbial agent capable of rapidly fermenting and decomposing; the microbial agent is a universal self-made cultured compound microbial agent, which contains various high-quality microorganisms with special functions, such as photosynthetic bacteria, azotobacter, phosphate and potassium solubilizing bacteria, bacillus mucilaginosus, bacillus subtilis, lactobacillus, saccharomycetes, high-temperature-resistant actinomycetes and the like; the microbial inoculum is mixed, fermented and compounded together, is not antagonistic and can be cooperated with each other, and is a compound microbial fermentation strain; the effective viable count is more than 15 hundred million/g and can reach more than 20 hundred million/g at most; the function is comprehensive, and the fermentation technology is added into the oily sludge organic material, can rapidly heat up, deodorize, dehydrate and thoroughly decompose, has good effects, is suitable for rapidly treating the oily sludge with the water content of 80 percent, and is a high-temperature and quick-acting fermentation technology; the method adopts mechanized full-automatic control high-temperature sealed fermentation equipment, and the high temperature in the equipment comes from the principle of using electricity to heat oil, and a high-temperature rapid fermentation method of utilizing oil electricity to conduct heat can enable the temperature to rise to 80-100 ℃ rapidly; harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge are effectively killed by using the high temperature of 100 ℃; the fermentation time of the whole oily sludge in the fermentation machine is shortened to 8 to 12 hours; the method effectively overcomes the defects that the traditional strip-stack aerobic fermentation process occupies large area and has long fermentation time, which generally needs 20 to 30 days.
The innovation of the technology of the invention is that: the treatment and disposal time of the oily sludge is short, the whole treatment and fermentation time is shortened to 8-12 hours, and the effect is good; the oily sludge with the water content of 80 percent can be manufactured into a useful organic matter regeneration clean fuel product at one time, and the national principle that the dangerous solid waste and sludge treatment should be followed by reducing the sludge amount from the source is realized; the oily sludge of the sewage treatment plant does not need to be sent to a refuse landfill for landfill, so that a large amount of land resources can be saved, and the environmental protection is facilitated; the occupied area is small, a factory can be arranged near a sewage treatment plant, and the transportation amount and the transportation cost for transporting the oily sludge can be greatly saved; low production cost and good economic benefit.
Compared with other domestic oily sludge treatment technologies, the method comprises the following steps:
1. compared with the domestic traditional oily sludge treatment method:
at present, various methods for treating the oily sludge with the water content of 80 percent are available in China; respectively as follows: technologies for implementing treatment and disposal of oily sludge include screening fluidization, conditioning, centrifugation, incineration, chemical hot washing, thermal desorption, composting, bioreactors, solvent extraction and the like, oily sludge generated in the domestic oilfield exploitation process generally adopts concentration dehydration, solidification, landfill treatment, catalytic cracking and the like, and the common defect of the existing treatment technologies is that heat energy contained in oily sludge with high economic value cannot be recycled; the invention has the technical innovation that the heat energy in the oily sludge can be utilized, a high-temperature rapid fermentation method is adopted to treat the oily sludge, the time is short, the treatment and fermentation time of the whole oily sludge is 8-12 hours, and the effect is good; the oily sludge with the water content of 80 percent can be manufactured into a regenerative clean fuel powder product of organic matters at one time, so that the national principle that sludge treatment and disposal are subject to the reduction of sludge from the source is realized; the stabilization, harmlessness, reduction and resource comprehensive utilization of the oily sludge are realized, the harm is turned into the benefit, the oily sludge with the water content of 80 percent does not need to be sent to a refuse landfill for landfill treatment, a large amount of land resources occupied by the oily sludge in the landfill process can be saved, and the treatment technologies such as landfill, incineration, blending combustion, solidification and the like are prioritized.
2. Compared with the pretreatment dehydration method of the oily sludge; wherein: the sludge concentration usually adopts two methods of gravity concentration and mechanical concentration, mechanical dehydration is carried out, and the commonly used mechanical sludge dehydration modes are a pressure filtration type and a centrifugal type, wherein the pressure filtration type mainly refers to a plate frame type and a belt type; a dehydration method, a concentration dehydration method;
the existing oily sludge treatment dehydration method mainly adopts a plate-frame mechanical dehydration method, and is characterized in that oily sludge with the water content of 80 percent conveyed by a sewage treatment plant is conveyed to a stacking yard, a plate-frame filter press is generally adopted for secondary dehydration treatment, and as the oily sludge with the water content of 80 percent has high viscosity, the dehydration can not be carried out by directly adopting the filter press, the oily sludge must pass through a sludge regulating water tank in the earlier stage of filter pressing, the oily sludge is subjected to alkene release degree regulation by using water to regulate the concentration of the oily sludge, and simultaneously a plurality of chemical agents are added into a regulating water tank, and after the demulsification treatment is carried out on the oily sludge by using the chemical agents, the oily sludge is conveyed to the filter press by using a water pump for filter pressing dehydration; the dewatered oily sludge is subjected to other process treatments, and simultaneously, a large amount of secondary sewage is generated in the filter pressing dewatering process, the sewage treatment is required, and the sewage is discharged after reaching the standard; a large amount of water resources are consumed in the treatment process, the treatment process does not accord with the regulation of national water-saving policy and the requirement of national environmental protection policy, the treatment time is too long, and the treatment cost is high.
The fly ash is selected as a raw material of a blender for treating the oil-containing sludge with the water content of 80 percent, and the adsorption effect, the flocculation precipitation and the filtration interception of the fly ash are mainly utilized; the adsorption effect of the fly ash comprises physical adsorption and chemical adsorption, wherein the physical adsorption means that the adsorption is generated between the fly ash and pollutant molecules of an adsorbate through intermolecular attraction, and the effect is determined by the porosity and the specific surface area of the fly ash; the chemical adsorption means that the fly ash contains a large amount of active ingredients of aluminum, iron and silicon, and can strongly adsorb most of colloid particles with negative electricity in the water contained in the oily sludge to generate flocculation; in addition, the fly ash contains coagulant aids, such as nickel, cobalt, arsenic, sodium, lithium and calcium, so that the sedimentation of the fly ash can be promoted; the chemical adsorption is characterized by strong selectivity, and under the common condition, the physical adsorption and the chemical adsorption exist at the same time, but the advantages of the physical adsorption and the chemical adsorption are different under different conditions of pH value and temperature, so that the adsorption performance of the fly ash is changed; in addition, as the fly ash is a mechanical mixture of various particles and has high porosity, when the moisture in the oily sludge passes through the fly ash, the fly ash can filter and retain all suspended matters;
the main influence factors of the fly ash in the process of treating the high water content of the oil-containing sludge include the following aspects: (1) The fly ash has small particle size fineness and large specific surface area, the finer the particle size of the fly ash is, the larger the specific surface area is, and the better the treatment effect on the water contained in the oil-containing sludge is; (2) chemical components of the fly ash: the content of active substances of SiO and A1O in the fly ash is higher, which is beneficial to chemical adsorption; (3) pH value of the solution: the pH value directly influences the treatment effect of water in the oily sludge, but the influence result of the pH value is related to the property of adsorbate; (4) temperature: research shows that the lower the temperature is, the higher the removal rate of harmful substances of the fly ash to the water in the oil-containing sludge is; (5) Properties of adsorbates: the solubility, molecular polarity, molecular weight and concentration of pollutants containing high water in the oily sludge all influence the water treatment effect of the oily sludge; the larger the molecular weight, the smaller the solubility, the better the treatment effect.
The invention selects chlorine dioxide as a disinfection, deodorization and bactericide in the treatment of oil-containing sludge with water content of 80 percent, wherein the chlorine dioxide is a product prepared by the action of sodium chlorate, sulfuric acid and methanol or the action of sodium chlorate and sulfur dioxide; chlorine dioxide is prepared by reducing chlorate serving as a raw material in a sulfuric acid medium; has the functions of sterilization, bleaching, deodorization, disinfection and fresh keeping; the action mechanism is mainly oxidation, the electronic structure of the chlorine dioxide molecule is in an unsaturated state, the outer layer has 19 electrons, the chlorine dioxide molecule has strong oxidation, and the chlorine dioxide molecule mainly attacks atomic groups (such as enzyme and sulfide containing sulfydryl and chloride) rich in electrons (or supplying electrons) and forcibly grazes the electrons to enable the electrons to become substances losing activity and changing properties, so that the aim is fulfilled;
1. the chlorine dioxide has stronger adsorption and penetration capacity on cell walls, and releases atomic oxygen to oxidize enzyme containing sulfydryl in cells to play a role in sterilization;
2. the bleaching of chlorine dioxide is to release atomic oxygen and generate hypochlorite to decompose pigment; the bleaching agent is used as a bleaching agent to replace chlorine and chlorate, so the effect is more comprehensive;
3. the deodorization effect of chlorine dioxide is that chlorine dioxide can generate dehydration reaction with odor substances (such as H2S, -SOH, -NH 2) and make the odor substances quickly oxidized and converted into other substances, and simultaneously kill microorganisms without reacting with fatty acid; the chlorine dioxide has a safety effect, cyanide can be oxidized into carbon dioxide and nitrogen, namely 2ClO2+2CN =2CO2+ N2+2Cl, when the concentration of the cyanide is 3.0mg/L, the dosage of the chlorine dioxide is 5.0mg/L, and the removal rate of the cyanide is generally more than 85%; the advantages that a large number of foreign experimental studies show that chlorine dioxide is a safe and nontoxic disinfectant, has no 'three-cause' effect (carcinogenesis, teratogenicity and mutagenicity), and does not generate chlorination reaction with organic matters to generate organic chloride or other toxic substances which can generate 'three-cause' effect in the disinfection process; but because chlorine dioxide has extremely strong oxidizing power, the chlorine dioxide is not used at high concentration (> 500 ppm); when the concentration is lower than 100ppm, the composition does not have any influence on human bodies, including physiological and biochemical influences; has no sensitization to skin; therefore, chlorine dioxide is also internationally recognized as a safe, non-toxic, green sanitizer.
The invention selects polyacrylamide as a flocculating agent for treating water contained in oil-containing sludge with water content of 80%, wherein the polyacrylamide is named as the Chinese alias: flocculant No. 3, PAM for short; polyacrylamide is also known as a No. three coagulant; the polyacrylamide is divided into anionic polyacrylamide, cationic polyacrylamide, nonionic polyacrylamide and amphoteric polyacrylamide; english name: PAM (acrylamide), abbreviation: PAM polyacrylamide is a water-soluble linear high molecular polymer which is formed by polymerizing Acrylamide (AM) monomers through free radical initiation, is insoluble in most organic solvents, has good flocculation property, can reduce the frictional resistance between sludge moisture, and can be divided into four types of non-ions, anions, cations and amphiprotic types according to the ionic characteristics; the mesh number of polyacrylamide is: the mesh number refers to the granularity or thickness of the material, is the number of squares on a unit area, and is generally defined as the number of meshes in an area of 1 inch x1 inch, namely the mesh number of the screen; for example, 600 meshes are 600 square meshes per square inch, the mesh size of polyacrylamide is generally 20-80 meshes, namely 0.85-0.2 mm, the mesh size of granular polyacrylamide is the mesh size, the mesh size of powdery polyacrylamide can be controlled to be about 100 meshes, and polyacrylamide with larger mesh size is easier to dissolve; the polyacrylamide is white powder or small granule with density of 1.32g/cm 3 (23 ℃) with a glass transition temperature of 188 ℃ and a softening temperature of approximately 210 ℃, which generally contains a small amount of water during drying, which quickly draws up water from the environment during drying, the homopolymer isolated by freeze-drying is a white, fluffy, non-crystalline solid, but when precipitated from solution and dried is a glassy, partially transparent solid, the fully dried polyacrylamide PAM is a brittle white solid, the commercial polypropylene PAMAmide drying is usually done under mild conditions; typically, the water content is five to fifteen percent, and the polymer film prepared by casting on a glass plate is a transparent, hard, brittle solid; the three-dimensional structure is mainly atactic; thermal stability: the material is easy to decompose when the temperature exceeds 120 ℃; solubility: dissolving in water, not dissolving in organic solvent such as benzene, toluene, ethanol, acetone, esters, etc., and dissolving in ethylene glycol, glycerol, formamide, lactic acid, and acrylic acid by about 1%; toxicity: is nontoxic; corrosion: no corrosion; moisture absorption: the solid is hygroscopic.
The invention selects the special strains for fermenting the agricultural sludge as the fermentation microbial inoculum for treating the oily sludge with the water content of 80 percent, and the product is a biological preparation developed by high-tech biotechnology in China (Taiwan) and contains high-concentration nonpathogenic beneficial microorganisms and is added with a plurality of enzymes capable of decomposing various macromolecular substances; the microorganism in the product can produce digestive enzyme in the fermentation process to decompose organic matters in the fermented sludge; the concentrated product is added in the fermentation process to supplement original strains and strengthen the decomposition of sludge organic matters so as to generate humus, and is suitable for sludge fermentation; the components are composite beneficial bacteria, the property is powder, and the total number of the live bacteria is more than or equal to 1.0 multiplied by 109cfu/g; the action mechanism is that under the aerobic condition, soluble organic matters in the fermentation materials penetrate through cell walls and cell membranes of microorganisms and are absorbed by the microorganisms; the solid and colloid organic matter is attached to the outside of microbe, and the microbe secretes extracellular enzyme to decompose it into soluble matter and permeate into cell, so that the microbe can metabolize to oxidize partial organic matter into simple inorganic matter and release energy; the microorganisms in the fermentation generate a large amount of heat in the decomposition process to heat the fermentation materials; this high temperature is necessary for rapid decomposition and is beneficial for destroying weed species, insect larvae, harmful bacteria, and inhibiting the growth of certain diseases that produce harmful microorganisms that inhibit the normal growth of plants. The addition of the fermenting microbial flora can improve the decomposition speed and efficiency, because the flora is a mixture of high-concentration bacteria and fungi which are screened, domesticated, cultured and improved; the strains are selected to better survive and propagate, simultaneously produce enzyme and decompose organic waste, thereby accelerating the decomposition of organic matters in the fermentation generation process; the standard concept for decomposing lignocellulosic bacteria is to first open the fibrous structure to make the sugars available for metabolism by different microorganisms; microorganisms release sugars from cellulose, hemicellulose, proteins, starch and other carbohydrates into fermentation products by using cellulase, xylanase, amylase, protease, enzymes for decomposing lignin and the like; the growth of the target bacteria in the fermentation process is strengthened, so that the growth of mixed bacteria can be effectively inhibited, and the generation of odor and the generation of harmful substances are prevented; the fermentation characteristics are as follows: (1) Certain heat is generated by the device, the high temperature duration is long, and the device can achieve harmlessness without an external heating source; (2) Various organic substances which are difficult to degrade are decomposed, the fermented materials are humified to a higher degree, and the available nutrients are improved; (3) The product is tasteless and odorless, has loose texture, low water content and small volume weight, so that organic matters generated in the fermentation process of the sludge provide food for microorganisms, and the microorganisms can generate nitrogen, phosphorus and potassium while the microorganisms take the food; can be used as the raw material of organic fertilizer.
The invention selects various high-quality microbial strains and ferment to mix, domesticate, culture and reactivate into a microbial agent which is used as a rapid leavening agent of oily sludge with the water content of 80 percent and is an activating microbial agent capable of rapidly fermenting and decomposing; the microbial agent is a universal self-made cultured compound microbial agent, which contains various special-function photosynthetic bacteria, nitrogen-fixing bacillus, pseudomonas fluorescens, phosphate-solubilizing potassium-solubilizing bacteria, colloidal bacillus, bacillus subtilis, lactobacillus, saccharomycetes, high-temperature-resistant actinomycetes and other microorganisms; the microbial inoculum is mixed, fermented and compounded together, is not antagonistic and can be cooperated with each other, and is a compound microbial fermentation strain; the effective viable count is more than 15 hundred million/g and can reach more than 20 hundred million/g at most; the function is strong, and the organic material can be quickly heated, deodorized and dehydrated at the normal temperature of about 15 ℃ and is completely decomposed in about 7 days after being added into the oily sludge organic material; the fermentation agent has comprehensive functions and good effect, not only has strong decomposition effect on sludge materials, but also breeds a large number of functional bacteria and generates a plurality of specific metabolites such as hormone and antibiotic in the fermentation process, and the nutrients are changed from an ineffective state and a slow effective state into an effective state and a quick effective state; the oil-containing sludge is humified and fermented to generate a large amount of humic acid, contains various auxin, amino acid, enzyme and antibiotic substances and functional substances capable of promoting the healthy growth of plants, thereby stimulating the growth and development of crops, improving the disease resistance, drought resistance and cold resistance of the crops, and after functional bacteria enter soil, fixing nitrogen, dissolving phosphorus and potassium, increasing soil nutrients, improving the soil structure and improving the fertilizer efficiency utilization rate; the oily sludge can be quickly decomposed and peculiar smell can be eliminated, the derivative of the oily sludge after fermentation treatment can be used as an organic matter regeneration clean fuel and is suitable for a coal-fired power plant as a combustion raw material, and the additional value of the oily sludge derivative product is improved.
In the invention, in the process of treating the oily sludge with water content of 80%, quicklime powder is used as an blender for disinfection and sterilization, ferrous sulfate is used as a reducing agent, magnesium sulfate is used as a ferrous iron retention agent, and calcium superphosphate is used as a deodorant, so that the oily sludge can be fully decomposed, and the aims of quickly deodorizing, disinfecting and sterilizing are achieved.
The invention relates to a method for producing regenerated clean fuel by using oily sludge, which comprises the following steps of mixing and stirring the oily sludge with the water content of 80%, fly ash powder, forestry waste powder, quick lime powder, ferrous sulfate, magnesium sulfate, polyacrylamide and chlorine dioxide uniformly by a double-shaft humidifying stirrer in proportion, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, and the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding a sludge special fermentation strain and a thermophilic high-temperature resistant active bacteria composite flora agent in proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, activating the activity of thermophilic high-temperature resistant composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by using the activity function of the thermophilic high-temperature resistant composite flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, so that harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge are effectively killed; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; aging, cooling, crushing and screening the fermented oily sludge clinker to prepare mixed powder with the particle size of less than 0.02 mm; then the uniformly mixed powder is conveyed to a special storage silo and is packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product; thereby solving the problem of treatment and disposal of the oily sludge with the water content of 80 percent, creating a new technical approach for the treatment and disposal of the oily sludge, and laying a good favorable foundation for the resource comprehensive utilization of the oily sludge; realizes the resource recycling of the oily sludge so as to reduce the pollution to the natural environment.
The clean fuel regenerated from the oily sludge produced by the technology of the invention has various technical indexes meeting the requirements of national low-quality coal after the inspection of the quality inspection departments stipulated by the nation.
The quality supervision inspection station for coal products supervised by Guangdong province technology has the following inspection results:
Figure RE-GDA0003832416250000141
the detection basis of the clean fuel regenerated from the oily sludge is as follows: refer to the relevant provisions of GB474-1996, GB/T211-1996, GB/T212-2001, GB/T213-2003, GB/T214-1996.
Due to the adoption of the technical scheme, the technology has the following advantages and effects:
a) The treatment and disposal time of the oily sludge with the water content of 80% is short, and the effect is good; the oily sludge with the water content of 80 percent can be manufactured into an organic matter renewable fuel product at one time, and the national principle that sludge treatment and disposal are subject to the reduction of sludge from the source is realized; the renewable fuel made by using the oily sludge provides a technology with good economic benefit for the resource comprehensive utilization of the oily sludge and other combustible wastes, thereby not only solving the problem that the oily sludge needs to occupy a large amount of land resources in the landfill process, but also solving the problem of environmental pollution caused by the oily sludge;
b) The oily sludge of the sewage treatment plant does not need to be sent to a refuse landfill for landfill, so that a large amount of land resources can be saved, and the ecological environment can be protected;
c) A large amount of transport capacity and transport cost can be saved, and the economic benefit is good;
d) The oily sludge organic matter renewable fuel product is a renewable product composed of multiple elements, wherein the oily sludge, fly ash and forestry wastes are used as main raw materials, and a sealed high-temperature fermentation machine is adopted to ferment with a special fermentation strain for sludge and a thermophilic high-temperature resistant active bacterium compound microbial agent;
e) A new technical route is created for the treatment and disposal of the oily sludge, and a good favorable foundation is laid for the resource comprehensive utilization of the oily sludge;
f) The problem of secondary environmental pollution caused by oily sludge to urban environmental sanitation is solved, and the environment is protected; meets the relevant regulations of the State Federal for modification 2011 No. 461 on further strengthening sludge treatment and recycling comprehensive utilization;
g) Simple production process, no three-waste discharge, meeting the national requirement spirit of circular economy, energy conservation, emission reduction and environmental protection, and the glass has the advantages of less investment, quick visual effect, low cost and good benefit, and is suitable for various levels of factories.
Detailed Description
Example 1
The oily sludge is the combination of activated sludge generated by the treatment of industrial wastewater of an oil refinery, electroplating wastewater, oily wastewater and domestic sewage in the process of petroleum mechanical processing by flotation, filtration, flocculation and chemical methods, and oily sludge of bottom mud of a crude oil separation tank, floating slag of a flotation tank and bottom mud of a crude oil tank; the oily sludge has various types, including: waste drilling mud generated in the process of petroleum exploitation, oil-water and hydrocarbon-water mixture generated in the process of cleaning mineral oil storage and transportation facilities, oily sludge generated by storage facilities, oil-water solid matter separators, water accumulation tanks, ditches and other transportation pipelines, sewage pools and rainwater collection pipelines in the process of primary petroleum refining, oily sludge generated by oil separation pools in the process of petroleum refining, and gasoline refining process
Sludge generated in the treatment process of waste water and cooling waste water, scum generated in a dissolved air flotation process in a petroleum refining process, spilled waste oil or emulsion generated in a petroleum refining process, oily sludge generated in a cleaning process of a petroleum refining heat exchanger tube bundle, clarified slurry tank bottom sediment in a petroleum refining process, residue generated in an oil inlet pipe filtering or separating device in a petroleum refining process, waste filtering medium generated in a petroleum refining process, waste mineral oil and oil sludge generated in a centralized disassembling process of an internal combustion engine, an automobile and a ship, waste mineral oil and oil sludge generated in a honing, grinding, polishing and process, waste kerosene, diesel oil and other solvent oils generated in a cleaning process of metal parts and a refining process by petroleum and kerosene, waste mineral oil generated in a surface hardening process by using quenching oil, waste mineral oil generated in a rolling process by using rolling oil, cooling agent and acid, mineral oil generated in a tin plating and recovery process, waste oil generated in a separation facility, scum and sludge generated in a waste oil treatment process, waste mineral oil generated in a rubber production process, waste mineral oil sludge generated in a regeneration process, waste oil sludge generated in a purification process, waste oil generated in a waste oil flotation process, and waste oil generated in a regeneration process, and flocculating residue generated in a waste oil purification process, and flocculating residue generated in a waste oil recovery process; standby;
fly ash is a volcanic ash-like mixed material formed by high-temperature combustion of coal powder; coal is ground into coal powder with the particle size of less than 100 microns by a thermal power plant, preheated air is sprayed into a hearth to be combusted in a suspension state, high-temperature flue gas mixed with a large amount of non-combustible substances is generated, and the coal powder is collected by a dust collecting device to obtain fly ash; magnetic separation, drying and screening are carried out to prepare powder with the particle size of less than 0.02 mm; standby;
forestry wastes, namely forestry felling residues, wood making residues and processing residues, such as branches, treetops, barks, leaves, roots and rattans, shrubs, wood making truncations, slabs, laths, wood and bamboo truncations, sawdust, crushed veneers, wood cores, wood shavings, wood blocks, thin bamboo strips, leftover bits and waste residues, are crushed, sorted, magnetically separated, dried, crushed, ground and screened to prepare powder with the particle size of less than 5 mm; standby;
calcining limestone at high temperature, crushing, sorting, crushing, grinding and sieving to prepare powder with the particle size of less than 0.02 mm; standby; taking 65kg of the prepared oily sludge with the water content of 80%, 35kg of fly ash powder, 25kg of forestry waste powder, 13kg of quick lime powder, 8kg of ferrous sulfate, 13kg of magnesium sulfate, 0.3kg of polyacrylamide and 0.3kg of chlorine dioxide, and uniformly mixing and stirring by adopting a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.01kg of sludge special fermentation strain and 0.02kg of thermophilic high-temperature resistant active bacteria composite flora agent according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by using the activity function of the thermophilic composite flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, so that harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge are effectively killed; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; aging, cooling, crushing and screening the fermented oily sludge clinker to prepare mixed powder with the particle size of less than 0.02 mm; and then the uniformly mixed powder is conveyed to a special storage silo and packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product.
Example 2
75kg of oily sludge with the water content of 80 percent, 25kg of fly ash powder, 30kg of forestry waste powder, 18kg of quick lime powder, 13kg of ferrous sulfate, 18kg of magnesium sulfate, 0.6kg of polyacrylamide and 0.6kg of chlorine dioxide in the embodiment 1 are taken and mixed and stirred uniformly by a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.05kg of sludge special fermentation strain and 0.06kg of thermophilic high-temperature resistant active bacteria composite microbial inoculum according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic composite microbial flora, and accelerating the rapid degradation of organic matters in the industrial sludge and the formation of humus by using the activity function of the thermophilic composite microbial flora; the fermentation time of the whole industrial sludge in the fermentation machine is 8-12 hours, so that harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the industrial sludge are effectively killed; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; aging, cooling, crushing and screening the fermented oily sludge clinker to prepare mixed powder with the particle size of less than 0.02 mm; and then the uniformly mixed powder is conveyed to a special storage silo and packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product.
Example 3
66kg of oily sludge with the water content of 80 percent, 26kg of fly ash powder, 26kg of forestry waste powder, 14kg of quick lime powder, 10kg of ferrous sulfate, 15kg of magnesium sulfate, 0.4kg of polyacrylamide and 0.4kg of chlorine dioxide in the embodiment 1 are taken and mixed and stirred uniformly by a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.03kg of sludge special fermentation strain and 0.04kg of thermophilic high-temperature resistant active bacteria composite microbial inoculum according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by using the activity function of the thermophilic composite microbial flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, so that harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the industrial sludge are effectively killed; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; aging, cooling, crushing and screening the fermented oily sludge clinker to prepare mixed powder with the particle size of less than 0.02 mm; and then the uniformly mixed powder is conveyed to a special storage silo and packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product.
Example 4
68kg of oily sludge with the water content of 80 percent, 30kg of fly ash powder, 28kg of forestry waste powder, 15kg of quick lime powder, 12kg of ferrous sulfate, 16kg of magnesium sulfate, 0.5kg of polyacrylamide and 0.5kg of chlorine dioxide in the embodiment 1 are taken, and are mixed and stirred uniformly by a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, and the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge into a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ by using oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.02kg of sludge special fermentation strain and 0.03kg of thermophilic high-temperature-resistant active bacteria composite microbial inoculum according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic composite microbial flora, and accelerating the rapid degradation of organic matters in the industrial sludge and the formation of humus by using the activity function of the thermophilic composite microbial flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, so that harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the industrial sludge are effectively killed; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; aging, cooling, crushing and screening the fermented oily sludge clinker to prepare mixed powder with the particle size of less than 0.02 mm; and then the uniformly mixed powder is conveyed to a special storage silo, and is packaged by a full-automatic electronic metering weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product.
Example 5
72kg of oily sludge with the water content of 80 percent, 33kg of fly ash powder, 30kg of forestry waste powder, 16kg of quick lime powder, 11kg of ferrous sulfate, 17kg of magnesium sulfate, 0.6kg of polyacrylamide and 0.6kg of chlorine dioxide in the embodiment 1 are taken, and are mixed and stirred uniformly by a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.04kg of sludge special fermentation strain and 0.05kg of thermophilic high-temperature resistant active bacteria composite microbial inoculum according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by using the activity function of the thermophilic composite microbial flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, so that harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge are effectively killed; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; aging, cooling, crushing and screening the fermented oily sludge clinker to prepare mixed powder with the particle size of less than 0.02 mm; and then the uniformly mixed powder is conveyed to a special storage silo and packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, aged and harmless organic matter regenerated clean fuel product.

Claims (7)

1. The regenerated clean fuel produced by the oily sludge is characterized by being prepared from the following raw materials in parts by weight:
Figure FDA0003741835000000011
the oily sludge is the combination of activated sludge generated by the industrial wastewater of an oil refinery, electroplating wastewater, oily wastewater and domestic sewage generated in the petroleum mechanical processing process and the oily sludge of the bottom sludge of a crude oil separation tank, floating slag of a flotation tank and the bottom sludge of a crude oil tank after the activated sludge is treated by flotation, filtration, flocculation and chemical methods;
the fly ash powder is a volcanic ash-like mixed material formed by high-temperature combustion of coal powder; coal is ground into coal powder with the particle size of less than 100 microns by a thermal power plant, preheated air is sprayed into a hearth to be combusted in a suspension state, high-temperature flue gas mixed with a large amount of non-combustible substances is generated, and the coal powder is collected by a dust collecting device to obtain fly ash; magnetic separation, drying and screening are carried out to prepare powder with the particle size of less than 0.02 mm;
the forestry waste powder is forestry felling residues, wood making residues and processing residues, and comprises branches, treetops, barks, leaves, roots and rattans, shrubs, wood making truncations, slabs, laths, wood bamboo truncations, saw dust, crushed veneers, wood cores, wood shavings, wood blocks, thin bamboo strips, leftover materials and waste residues, and the powder with the particle size of less than 5mm is prepared by crushing, sorting, magnetic separation, drying, crushing, grinding and screening;
the quick lime powder is prepared by calcining limestone at high temperature, crushing, sorting, crushing, grinding and screening to obtain powder with the particle size of less than 0.02 mm;
the polyacrylamide is white powder or small particles, and the density is 1.32g/cm 3
2. A method for manufacturing regenerated clean fuel produced by oily sludge is characterized by comprising the following steps: mixing and stirring oil-containing sludge with water content of 80%, fly ash powder, forestry waste powder, quicklime powder, ferrous sulfate, magnesium sulfate, polyacrylamide and chlorine dioxide uniformly according to the proportion, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8;
conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding a sludge special fermentation strain and a thermophilic high-temperature resistant active bacteria composite flora agent in proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, activating the activity of thermophilic high-temperature resistant composite microbial flora, and accelerating the rapid degradation of organic matters in the oily sludge and the formation of humus by using the activity function of the thermophilic high-temperature resistant composite flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, and the method is used for killing harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge;
the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved;
the fermented oily sludge clinker is cooled, crushed and screened to prepare mixed powder with the particle size of less than 0.02mm, and the mixed powder is conveyed to a special storage silo.
3. The method for producing regenerated clean fuel by using oily sludge according to claim 2, characterized in that the fermentation of the oily sludge adopts a mechanical full-automatic high-temperature sealed fermentation device, the high temperature in the device is derived from the principle of heating oil by electricity, and an oil-separating layer is arranged in the device and the fermentation method of heating by oil electric heat conduction is adopted.
4. The method for producing a renewable clean fuel by using oily sludge according to claim 2, wherein the fermentation strain of the oily sludge comprises a mixture of a sludge-dedicated fermentation strain and a thermophilic high-temperature resistant active bacteria composite microbial inoculum in proportion.
5. The method for producing a recycled clean fuel from oily sludge as claimed in claim 2, wherein the mixing and stirring of the oily sludge is carried out by a double-shaft humidifying mixer.
6. The method for manufacturing the renewable clean fuel produced by the oily sludge according to the claim 2, characterized in that the powder material conveyed to the special storage silo is packaged by a full-automatic electronic metering weighing packaging machine system.
7. The method for manufacturing the regenerated clean fuel produced by the oily sludge according to the claim 2, which is characterized by comprising the following steps:
taking 65-75 parts by weight of oily sludge with water content of 80%, 25-35 parts by weight of fly ash powder, 25-30 parts by weight of forestry waste powder, 13-18 parts by weight of quick lime powder, 8-13 parts by weight of ferrous sulfate, 13-18 parts by weight of magnesium sulfate, 0.3-0.6 part by weight of polyacrylamide and 0.3-0.6 part by weight of chlorine dioxide, and uniformly mixing and stirring by adopting a double-shaft humidifying stirrer, wherein: the water content of the mixture is controlled to be 45-65%, the materials are held by hands to form a cluster without water drops, the materials are loosened by hands, the carbon-nitrogen ratio is 25-30: 1, the pH value is 6-8; conveying the sludge to a sealed high-temperature fermentation machine by using a belt conveyer, starting a heating system, raising the temperature in the fermentation machine to 80-100 ℃ through oil and electric conduction heat, keeping the temperature for 2 hours, then cutting off the power, keeping the temperature between 60-80 ℃, simultaneously adding 0.01-0.05 weight part of sludge special fermentation strain and 0.02-0.06 weight part of thermophilic high-temperature resistant active bacteria composite flora agent according to the proportion for fermentation, adjusting a stirring system matched with the fermentation machine to an intermittent stirring function, simultaneously activating the activity of thermophilic high-temperature resistant bacteria composite microbial flora, and accelerating the rapid degradation of organic matters in the oil-containing sludge and the formation of humus by using the activity function of the thermophilic high-temperature resistant composite flora; the fermentation time of the whole oily sludge in the fermentation machine is 8-12 hours, and the method is used for killing harmful microorganisms, worm eggs, weed seeds and pathogenic bacteria in the oily sludge; the water vapor generated in the fermentation process is adsorbed by an activated carbon absorption box, and the specific surface area and the adsorption function of the activated carbon are utilized to adsorb and purify trace waste gas in the water vapor, so that the odorless colorless up-to-standard emission is achieved; the fermented oily sludge clinker is cooled, crushed and screened to prepare mixed powder with the particle size of less than 0.02mm, the mixed powder is conveyed to a special storage silo and packaged by a full-automatic electronic metering and weighing packaging machine system to prepare a stabilized, matured and harmless organic matter clean fuel product.
CN202210818694.4A 2019-07-19 2019-07-19 Regenerated clean fuel produced by using oily sludge and manufacturing method thereof Pending CN115287108A (en)

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