CN1872747A - System of innocent treatment for grease of oil - Google Patents
System of innocent treatment for grease of oil Download PDFInfo
- Publication number
- CN1872747A CN1872747A CNA200510072350XA CN200510072350A CN1872747A CN 1872747 A CN1872747 A CN 1872747A CN A200510072350X A CNA200510072350X A CN A200510072350XA CN 200510072350 A CN200510072350 A CN 200510072350A CN 1872747 A CN1872747 A CN 1872747A
- Authority
- CN
- China
- Prior art keywords
- oil
- greasy filth
- treatment
- petroleum
- grease
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000004519 grease Substances 0.000 title claims description 7
- 238000000034 method Methods 0.000 claims abstract description 23
- 230000008569 process Effects 0.000 claims abstract description 13
- 239000010779 crude oil Substances 0.000 claims abstract description 9
- 238000002156 mixing Methods 0.000 claims abstract description 4
- 238000004391 petroleum recovery Methods 0.000 claims abstract description 4
- 239000003921 oil Substances 0.000 claims description 17
- 238000002203 pretreatment Methods 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 5
- 239000002920 hazardous waste Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 11
- 238000000197 pyrolysis Methods 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 239000003208 petroleum Substances 0.000 abstract description 7
- 239000010802 sludge Substances 0.000 abstract description 6
- 238000007599 discharging Methods 0.000 abstract description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 19
- 239000003546 flue gas Substances 0.000 description 18
- 238000010304 firing Methods 0.000 description 17
- 230000009977 dual effect Effects 0.000 description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 13
- 239000007789 gas Substances 0.000 description 13
- 235000019198 oils Nutrition 0.000 description 13
- 238000002485 combustion reaction Methods 0.000 description 10
- 239000002918 waste heat Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000000428 dust Substances 0.000 description 7
- 230000007613 environmental effect Effects 0.000 description 7
- 238000002309 gasification Methods 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000012544 monitoring process Methods 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 235000011121 sodium hydroxide Nutrition 0.000 description 6
- 239000002585 base Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 238000005457 optimization Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 150000002013 dioxins Chemical class 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 206010017472 Fumbling Diseases 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000007233 catalytic pyrolysis Methods 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011499 joint compound Substances 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000013178 mathematical model Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 235000019476 oil-water mixture Nutrition 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000001149 thermolysis Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000006200 vaporizer Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
Landscapes
- Incineration Of Waste (AREA)
Abstract
This invention discloses a system for treating petroleum sludge produced during petroleum production and refinery. The system comprises a petroleum sludge pretreating system, a petroleum recovery system, a pyrolysis system, a off-gas treating system, a heat utilization system, and an automatic controlling system. The process comprises: pretreating the petroleum sludge, recovering crude oil, mixing, pyrolyzing, recovering the excess heat, treating the oss-gas, and discharging. The treated petroleum sludge does not contain petroleum or other harmful components, thus is environmentally friendly. The excess heat can be fully utilized, and the residue can be used as a pavement material.
Description
Technical field
The greasy filth that The present invention be directed in oil production and the refining process to be produced and a kind of process unit system that carries out harmless treatment.
Background technology
Greasy filth is the entrained mud of crude oil in oil production and the refining process, sand precipitation, oil extraction-generated waste water scum silica frost and bed mud, and the ground crude oil that produces in the drilling well, oil recovery process such as mixes at the pollutent of formation with earth, foreign material.After greasy filth enters environment, environment is polluted, classify Hazardous wastes as in " national Hazardous wastes register ", oil-containing must carry out harmless treatment above 3/1000ths greasy filth.About the processing of greasy filth, all pay much attention to countries in the world.At present institute generally employing be partition method, solidification method and biological degradation method.The partition method technical process is: oily sludge → stirring homogenizing → separation of liquefying → heat, this method energy Separation and Recovery part crude oil, but energy consumption is big, handle not thorough, isolated silt particle still contains certain petroleum substance, do not reach the requirement of burying of environmental regulations, also need further processing; The solidification method technical process is: oily sludge → storage tank → adding lime and diatomite → pressure filter, filter cake → refuse tip is stacked, this method cost height, and oil length height in the dried mud, waste is big, and aftertreatment is untimely to cause secondary pollution easily; Biological degradation method is to utilize microorganism that contained oily substance in the greasy filth is decomposed, and environmental factorss such as soil property, temperature, humidity are had relatively high expectations, and the cycle is long, has high input, and narrow application range domesticly also is in the technology stage of fumbling.
Summary of the invention
The invention provides and a kind of greasy filth is carried out the process unit system of harmless treatment and recycling, its system is composed as follows:
The greasy filth pretreatment system, petroleum recovery system, system for pyrolyzing and burning, exhaust treatment system, heat energy utilization system, automation control system.
Greasy filth pretreatment system: constitute by feeding system, concentration systems and mixing of materials system;
Petroleum recovery system: constitute by catalytic pyrolysis system, oil-water separation system, after-treatment system;
System for pyrolyzing and burning: constitute by charging system, pyrogenation incinerator, dual firing chamber, three combustion chambers;
Exhaust treatment system: constitute by quenching system, spray column, sack cleaner, activated carbon adsorber etc.;
Heat energy utilization system: constitute by superheater, economizer, waste heat boiler etc.;
Automation control system: constitute by data collecting system, Controlling System, burning regulation system, tail gas clean-up processing regulation system etc.;
System of innocent treatment for grease of oil technical process of the present invention: greasy filth pre-treatment → crude oil recovery → mixing is fed in raw material → pyrolytic incineration → UTILIZATION OF VESIDUAL HEAT IN → vent gas treatment → environment protection emission
The greasy filth of handling through the present invention no longer contains petroleum-type and other objectionable constituent, compliance with environmental protection requirements, and residue can be used as place mat roadbed material, material of construction or the like, has realized the purpose of minimizing that Hazardous wastes handles, innoxious, resource utilization.
Embodiment
Greasy filth pre-treatment and charging.Comprise two portions: the greasy filth pre-treatment and the pre-treatment of pyrolytic incineration greasy filth of reclaiming crude oil.Floorboard with high oil content greasy filth is sorted, and its each components contents is measured in chemical examination, and crude oil is wherein reclaimed.Floorboard with high oil content greasy filth barrier coarse filtration, to filterable greasy filth preheating, greasy filth when mud, oil, water stratification, is extracted the oil-water mixture on upper strata out with pump after preheating, enters gun barrel and separates.Simultaneously, oil removing bed mud and high-moisture percentage, low oil content greasy filth are transported to whizzer to dewater, make water ratio be lower than 50%, dehydration back greasy filth with burn after the slag trash chute of packing into, by lift it is transported to and adds material outlet, alternately pour feed bin into by switching mechanism, the rotary feeding of evacuating feeding units and distributor by two rollers adds in the body of heater continuously, distributor rotates material is spilt out equably, guarantees that material fully burns in incinerator.The waste liquid of centrifugation is stored, and concentrated solution sprays burning disposal by slush pump, and supernatant liquor is transported to sewage work.
Pyrolytic incineration.Incinerator adopts advanced pyrolytic gasification principle, fires indoor burning level and is followed successively by dryer section, pyrolysis section, burning zone, burning segment and cooling section from top to bottom.The greasy filth that enters a combustion chamber is at first at the flue gas drying of dryer section by the pyrolysis section rising, moisture evaporation wherein; Be decomposed into combustiblematerials such as carbon monoxide, gaseous hydrocarbons in the pyrolytic gasification section and form mixed flue gas, mixed flue gas is inhaled into dual firing chamber's burning; Residue behind the pyrolytic gasification enters burning zone and fully burns, and temperature is at 1100～1300 ℃, and its heat is used to provide pyrolysis section and dryer section institute energy requirement.The residue that burning zone produces enters cooling section after burning away through burning segment, by an air feed cooling of a combustion chamber bottom (residue preheating simultaneously a wind), be expelled in the water sealed tank of furnace bottom through the mechanical presses of fire grate, the block that is broken into below the 150mm, discharge through the wet type slag-tapping system.The mixed flue gas that pyrolytic gasification stove produces dirt enters secondary combustion chamber, through the secondary air oxygen supply, carries out oxygen-excess combustion, temperature is controlled at 1000 ℃ ± 50 ℃ in the stove, adopt temperature, pressure automatic control system, monitor in real time, make whole pyrolysis system be in little negative pressure attitude.A wind passes residual layer provides competent combustion-supporting oxygen to burning zone.Air goes upward to pyrolysis section after burning zone consumes a large amount of oxygen, and has formed the oxygen debt or anoxia condition that the pyrolytic gasification reaction takes place.Therefore, combustiblecomponents distributes in the indoor two-stage of energy that realized after pyrolysis of a combustion in the greasy filth: the cracking composition enters dual firing chamber and burns, residue is stayed the indoor burning of a combustion after the cracking, and the thermolysis of greasy filth, gasification, burning have formed along the running balance that moves downward direction.When feeding intake with the operation of dreg removing system continous-stable, the physical and chemical process of each conversion zone also continues to carry out in the stove, thereby has guaranteed the lasting normal operation of pyrolytic gasification stove.The 3T+E principle is adopted in secondary combustion, and flue gas enters dual firing chamber and adopts tangential entry, increases the less turbulence of gas in dual firing chamber; Ingress of dual firing chamber adopts secondary to mend wind, replenishes the oxygen in the flue gas, makes the fully burning under the oxygen enrichment of dual firing chamber, hot conditions of combustiblematerials that pyrolytic process produces.Flue gas surpasses 2 seconds in the residence time of dual firing chamber, and incineration temperature reaches about 900 ℃.The moving situation of flue gas in dual firing chamber makes dual firing chamber play the effect of cyclone dust removal simultaneously, and the dust of carrying secretly in the flue gas collects in the bottom of dual firing chamber greatly, discharges dual firing chamber by ash exhauster.Make when organic component thoroughly incinerates in the greasy filth, burning the formation condition of avoiding and destroyed pollutent on the important technology features such as mechanism, reducing atmosphere, flue dust generation and temperature of combustion, measure of control have been taked at pollutent formation mechanisms such as Dioxins, greatly reduce the growing amount of pollutents such as Dioxins, NOx, SOx, HCL, realized the clean burning of greasy filth.
Heat energy utilization: the waste heat boiler body is combined by a plurality of parts, comprises water wall, drum, generating tube tank nest, superheater, desuperheater and economizer etc.For improving the efficient of greasy filth waste gas of incineration boiler, taked multinomial design measure targetedly, as increasing furnace volume, reasonable Arrangement heat-transfer surface, use corrosion resistant material and coating etc., to raise the efficiency, avoid the high low temperature corrosion of each heating surface.Waste heat boiler is according to conditions such as design steam production, customer needs, and steam is delivered to steam distributor to be distributed, and can many-sidedly utilize.1, steam is introduced in the greasy filth producer, produced by interchanger and stablize thermal source (about 300 ℃), the preheating of fuel feeding mud, crude oil recovery are used; 2, steam can be used for plant area's production, heating for residential area, bathing, saves fire coal, reduces and pollutes; 3, utilize steam turbine generating etc.
Vent gas treatment: because greasy filth burning back generation dust and obnoxious flavour are (as SO
2, HCl, HF, NO
x, dioxin and heavy metal Hg, cadmium, lead etc.) contaminate environment, must dispose smoke eliminator and make fume emission up to standard.Flue gas through waste heat boiler adopts quenching apparatus to carry out reasonable controlled temperature, adopts technology such as semidrying deacidification temperature adjustment, bag-type dusting, charcoal absorption to satisfy flue gas purifying technique and discharges with environment protection standard.The total system major equipment includes pulping equipment, deacidification spray tower, sack cleaner, activated carbon filtration tower, air compressor.Caustic soda is added the Na (OH) that water is mixed with 20% concentration at fluid storage tank
2Solution is sent into alkali lye on demand by the screw feeder pump that alkali lye is atomized the droplet that device is atomized into 70～200um in the reaction tower through the nozzle at reaction tower top.Droplet is subjected to hot flue gas effect upwards, forms the high-density region that an alkaline droplet suspends, acidic substance HCl, SO in the flue gas near nozzle
2Neutralization reaction takes place Deng passing this when zone.It is 200 ℃ that flue gas is gone into the tower temperature, because the cooling effect of fogged lye drops to about 150 ℃ the water evaporation in the alkali lye simultaneously when going out tower.Flue gas behind the tower internal reaction is being carried resultant of reaction (NaCL, Na secretly
2SO
4Deng) dried powder dirt enter sack cleaner.Ash-laden gas enters ash bucket and middle casing, the thicker granule dust of a part under the guiding device effect natural subsidence in ash bucket, and be discharged into ash-transmission system from ash exhauster, played the effect that is subjected to dirt in advance, and other is adsorbed on the surface of filter bag than fine dust downwards with air-flow, and the clean gas after the filtration is passed cloth bag and entered upper box and be collected to air outlet tube and enter the activated carbon filtration tower.Flue gas after being purified is extracted out by induced draft fan and is entered atmosphere through chimney.The flying dust that dust-removal system is discharged adopts cement solidification to handle landfill.
Incineration system control
Incineration system control is mainly carried out centralized Control to whole burning process, from automatic feed to the wet type deslagging, from drying, the pyrolysis of rubbish, be burned to vent gas treatment, monitor from charging and to burn the control monitoring and the gas fume control monitoring waits each link all to monitor in real time, its concrete function can be considered the multiple information transmission, the overall monitor of incineration system and management, realize integrated etc., thereby reach sharing of information, resource and task.Burning Controlling System mainly is made of following subsystem:
1, data collecting system.The data of gathering mainly contain the continuous data of weighbridge; The vaporizer temperature; Furnace pressure; Furnace bottom pressure; Dual firing chamber's inlet temperature; Dual firing chamber's temperature out; The waste heat boiler out temperature; The waste heat boiler inlet outlet pressure differential; Waste heat boiler vapor pressure, temperature, flow, steam water-level; Feed temperature, flow; The sack cleaner inlet outlet pressure differential; The bag-type dust inlet temperature; Flue gas flow; Smoke evacuation CO, SO
2, NO
x, HCL content (online detection); Smoke content; Rotating speed of motor such as induced draft fan, gas blower, electric current etc.These data are gathered from the intelligent object of integrated transmitter, be sent to monitoring equipment in real time, for Controlling System and other regulation systems provide data by application program.
2, Controlling System.The control that this system mainly carries out has greasy filth discharging safety, and is crashproof; Crane quickens and parking stall control; Reinforced material level control; Dual firing chamber's temperature control; Waste heat boiler safety and blow ash control; Remove acid tower alkali lye and supply with control; Sack cleaner blows ash manipulation control etc.By this system, can monitor real-time information such as incinerator, boilers.
3, burn regulation system.This system regulates the inlet amount of feed system and the deslagging speed and the combustion air amount of rotary fire grate automatically according to the vapor temperature and the vapor pressure parameter of waste heat boiler, and the thermal load of control incinerator keeps the stable of main steam.In order to prevent to cause the incinerator overload, be provided with transfinite protection and warning function automatically because of the variation of greasy filth calorific value; Simultaneously according to CO in the tail gas and O
2The secondary air flow of content control dual firing chamber, make the CO content in the exhaust emissions up to standard.Control these parameters, guarantee the safe operation of total system.
4, the regulation system of tail gas clean-up processing.Pressure differential detection value that the with good grounds sack cleaner of the major control that this system carried out is imported and exported and set(ting)value are come the action of setting pulse sootblower; According to SO in the temperature of half dry type temperature adjustment tower outlet flue gas and the tail gas
x, deleterious acidic material such as HCL content regulate Na (OH)
2Addition, up to standard with the normal operation and the exhaust emissions that guarantee sack cleaner, when discharge harmful exceeds standard, system will write down automatically, print and report to the police, and these data are sent to database will preserve, for future vent gas treatment data are provided.
The management level function
Utilize the platform of plant area's local area network, real time data carried out comprehensive treating process,, mainly comprise the following aspects to realize many management functions:
1, data gathering and communication system
This system in time to collecting, store, analyze and handle from the production information at burning electricity generation scene, becomes the significant data of factory management infosystem, is used for the decision-making of production management, economic analysis, equipment control, all many-sides such as feed consumption management.To collection in worksite to information (by DCS or intelligent object) be sent to monitoring equipment by serial ports, and then these data are sent to database server by real-time Data Transmission technology and application program, put into real-time data base and historical data base, for WEB server calls data provide the data basis.And the staff can understand field data by browser, and on-the-spot various case is carried out Comprehensive Control and management.
2, burn Optimization Expert System
On the basis of setting up real-time data base and historical data base, can embed a small-sized burning Optimization Expert System again, incineration system is carried out condition diagnosing and Control Parameter Optimization.Condition diagnosing is core with optimizing subsystem with incinerator firing system mathematical model, with the knowledge base system of this model as expert systems, based on real-time monitoring parameter, greasy filth incinerator for thermal decomposition pyrolyzing, gasifying and incinerating operating mode is carried out analog calculation, adopt modeling method that the pyrolytic incineration operating mode is analyzed, and predicted burning operating mode in conjunction with the real time data library information, for Controlling System provides the open loop suggestion, improve the economic benefit of total system.
3, environmental protection competent authorities are to the remote supervisory of real time data
The remote communicating function that utilizes the internet links to each other with the Internet network with the Environmental Protection Agency network, realizes that environmental administration is current developing direction to the remote monitoring that greasy filth burns power plant's operation and pollutant emission concentration and total amount.Be the needs that adapt to the situation and develop, native system reservation port is interconnected with realization and Environmental Protection Agency's local area network.
Claims (3)
1, a kind of system of innocent treatment for grease of oil, its system is composed as follows:
The greasy filth pretreatment system, petroleum recovery system, system for pyrolyzing and burning, exhaust treatment system, heat energy utilization system, automation control system.
2, a kind of system of innocent treatment for grease of oil technical process: greasy filth pre-treatment → crude oil recovery → mixing is fed in raw material → pyrolytic incineration → UTILIZATION OF VESIDUAL HEAT IN → vent gas treatment → environment protection emission.
3, according to claims 1 described system of innocent treatment for grease of oil, according to claims 2 described system of innocent treatment for grease of oil technical process, take the specific embodiment of the present invention, carry out greasy filth and handle, realize the purpose of minimizing that Hazardous wastes handles, innoxious, resource utilization.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200510072350A CN100590083C (en) | 2005-05-31 | 2005-05-31 | System of innocent treatment for grease of oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200510072350A CN100590083C (en) | 2005-05-31 | 2005-05-31 | System of innocent treatment for grease of oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1872747A true CN1872747A (en) | 2006-12-06 |
| CN100590083C CN100590083C (en) | 2010-02-17 |
Family
ID=37483375
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200510072350A Expired - Fee Related CN100590083C (en) | 2005-05-31 | 2005-05-31 | System of innocent treatment for grease of oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100590083C (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103134054A (en) * | 2011-12-02 | 2013-06-05 | 华油惠博普科技股份有限公司 | Vehicle prying type oily sludge intelligent module processing system |
| CN103134053A (en) * | 2011-11-22 | 2013-06-05 | 上海巴安水务股份有限公司 | Drying incineration treatment method for sludge containing oil |
| CN107075395A (en) * | 2014-05-12 | 2017-08-18 | Dps布里斯托尔（控股）有限公司 | The waste treatment method at station is exploited for fossil fuel |
| CN107381995A (en) * | 2017-09-19 | 2017-11-24 | 来江 | A kind of oil-containing mud sand hazardous waste disposal system |
| CN107777847A (en) * | 2017-09-04 | 2018-03-09 | 重庆富燃科技股份有限公司 | Greasy filth is innoxious, recycling, the method for integrated treatment |
| CN108050522A (en) * | 2017-11-14 | 2018-05-18 | 松原市宁江区松城废旧资源再生利用有限公司 | A kind of serialization greasy filth environment-friendly treating process |
| CN108916889A (en) * | 2018-05-21 | 2018-11-30 | 永清环保股份有限公司 | A kind of dystopy greasy filth nonflame smouldering processing unit and processing method |
| CN109534653A (en) * | 2018-12-29 | 2019-03-29 | 重庆盎瑞悦科技有限公司 | A kind of front end sludge drying system in solid waste Thermal desorption accumulation of heat burning disposal |
| CN109631062A (en) * | 2019-02-22 | 2019-04-16 | 中国科学院力学研究所 | A kind of gas pulse soot blower cooling based on water mist |
| CN111298735A (en) * | 2020-02-12 | 2020-06-19 | 苏州垣瑞环境科技有限公司 | Self-circulation intelligent heat supply system for oil sludge resource utilization |
| CN112811770A (en) * | 2021-02-09 | 2021-05-18 | 天津泰姆生态环境科技有限公司 | Oil sludge treatment method |
-
2005
- 2005-05-31 CN CN200510072350A patent/CN100590083C/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103134053A (en) * | 2011-11-22 | 2013-06-05 | 上海巴安水务股份有限公司 | Drying incineration treatment method for sludge containing oil |
| CN103134054A (en) * | 2011-12-02 | 2013-06-05 | 华油惠博普科技股份有限公司 | Vehicle prying type oily sludge intelligent module processing system |
| CN107075395A (en) * | 2014-05-12 | 2017-08-18 | Dps布里斯托尔（控股）有限公司 | The waste treatment method at station is exploited for fossil fuel |
| CN107777847A (en) * | 2017-09-04 | 2018-03-09 | 重庆富燃科技股份有限公司 | Greasy filth is innoxious, recycling, the method for integrated treatment |
| CN107381995A (en) * | 2017-09-19 | 2017-11-24 | 来江 | A kind of oil-containing mud sand hazardous waste disposal system |
| CN108050522B (en) * | 2017-11-14 | 2019-08-20 | 松原市宁江区松城废旧资源再生利用有限公司 | A kind of serialization greasy filth environment-friendly treating process |
| CN108050522A (en) * | 2017-11-14 | 2018-05-18 | 松原市宁江区松城废旧资源再生利用有限公司 | A kind of serialization greasy filth environment-friendly treating process |
| CN108916889A (en) * | 2018-05-21 | 2018-11-30 | 永清环保股份有限公司 | A kind of dystopy greasy filth nonflame smouldering processing unit and processing method |
| CN109534653A (en) * | 2018-12-29 | 2019-03-29 | 重庆盎瑞悦科技有限公司 | A kind of front end sludge drying system in solid waste Thermal desorption accumulation of heat burning disposal |
| CN109631062A (en) * | 2019-02-22 | 2019-04-16 | 中国科学院力学研究所 | A kind of gas pulse soot blower cooling based on water mist |
| CN109631062B (en) * | 2019-02-22 | 2023-09-05 | 中国科学院力学研究所 | Air pulse soot blower based on water mist cooling |
| CN111298735A (en) * | 2020-02-12 | 2020-06-19 | 苏州垣瑞环境科技有限公司 | Self-circulation intelligent heat supply system for oil sludge resource utilization |
| CN112811770A (en) * | 2021-02-09 | 2021-05-18 | 天津泰姆生态环境科技有限公司 | Oil sludge treatment method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100590083C (en) | 2010-02-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100590083C (en) | System of innocent treatment for grease of oil | |
| CN103557526B (en) | Dangerous waste and medical waste incinerator complexes and incinerating method thereof | |
| US4753181A (en) | Incineration process | |
| CN109469903B (en) | Incineration treatment method for industrial solid waste | |
| US7611576B2 (en) | Method and plant for processing waste | |
| CN101963358B (en) | Combined treatment method for oilfield solid waste | |
| CN1259525C (en) | Method of processing refuse burning fly ash through cyclone furnace high temperature melting | |
| CN204006025U (en) | A kind of dangerous waste and medical waste incinerator complexes | |
| CN101561144B (en) | Clean incineration system of refuse and organic wastes and device thereof | |
| CN103363531A (en) | Whole-set hazardous waste incinerator device | |
| CN203628674U (en) | Whole-set hazardous waste incinerator device | |
| CN105716092A (en) | System treatment method for oil field oily sludge | |
| CN108455807A (en) | A kind of oily sludge harmless treatment device and method | |
| Brereton | Municipal solid waste—incineration, air pollution control and ash management | |
| US3859174A (en) | Recovery of potable water from sanitary waste using solid wastes and refuse as a heat source | |
| CN1800714A (en) | Fluidized bed incineration method for industrial organic waste liquid with high salt content | |
| CN1186559C (en) | Refuse gasifying incineration treatment method of rotary furnace siege | |
| CN104100980B (en) | A kind of small-sized rubbish charing combustion furnace | |
| CN103134054A (en) | Vehicle prying type oily sludge intelligent module processing system | |
| Winanti et al. | Utilization of municipal solid waste into electricity energy: A performance of PLTSa Bantargebang pilot project | |
| CN201078701Y (en) | Petroleum sludge grate firing helix grate incineration furnace | |
| CN102147114A (en) | House refuse thermal pyrolysis device | |
| CN107325830A (en) | A kind of rubbish and pyrolyzing sludge system and refuse disposal system | |
| CN101451708A (en) | Subcritical damp steam generating system by petroleum sludge innoxious energy-gathering treatment | |
| CN110260334A (en) | Waste incineration and system for cleaning fume |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C57 | Notification of unclear or unknown address | ||
| DD01 | Delivery of document by public notice |
Addressee: Hou Xiangming Document name: Notification of registration of the invention patent right |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHANG JUNLIN Free format text: FORMER OWNER: JIASHIJIADE (BEIJING) ENERGY ENGINEERING TECH CO., LTD. Effective date: 20110803 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20110803 Address after: 102200 Beijing city Changping District town Changping Xinyue No. 2 homes 1704 Patentee after: Zhang Junlin Address before: 102200 Beijing Changping District Science Park Road No. 10 Bai Fu Tuo ran Jia Yuan Building 5 1-304 Patentee before: Jiashijiade (Beijing) Energy Engineering Tech Co., Ltd. |
|
| DD01 | Delivery of document by public notice |
Addressee: Zhang Junlin Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice |
Addressee: Zhang Junlin Document name: Notification to Pay the Fees |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100217 Termination date: 20180531 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |