CN206156893U - Coal industry waste lye pollutes integrated control system - Google Patents

Coal industry waste lye pollutes integrated control system Download PDF

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Publication number
CN206156893U
CN206156893U CN201620756939.5U CN201620756939U CN206156893U CN 206156893 U CN206156893 U CN 206156893U CN 201620756939 U CN201620756939 U CN 201620756939U CN 206156893 U CN206156893 U CN 206156893U
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China
Prior art keywords
spent lye
lye
coal
pollutes
control system
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Inventor
姚国华
丁海荣
闫宁
闫朝友
孙振江
阎全国
刘艳军
张翔
黄垒
贺延利
陈德武
王利亭
殷浩
范公明
赵彬
牟鑫
毛雪强
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YIXING RONG SHENG DA ENVIRONMENTAL PROTECTION CO Ltd
Hualu Engineering and Technology Co Ltd
Pucheng Clean Energy Chemical Co Ltd
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YIXING RONG SHENG DA ENVIRONMENTAL PROTECTION CO Ltd
Hualu Engineering and Technology Co Ltd
Pucheng Clean Energy Chemical Co Ltd
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Priority to CN201620756939.5U priority Critical patent/CN206156893U/en
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Abstract

The utility model discloses a coal industry waste lye pollutes integrated control system, coal industry waste lye pollutes integrated control system is including useless lye recovery clean system and the waste lye system of recycling, useless lye recovery clean system includes: waste water catch basin, gravity separation ware, profit collecting pit, air supporting device, oil water separator, ozone and H2O2 unite oxidation unit, walnut shell filter, the waste water catch basin is connected to through the promotion of first pump the gravity separation ware, the gravity separation ware is connected the air supporting device, and the gravity separation ware is still connected through the overflow launder the profit collecting pit, the air supporting device is connected to oil water separator, oil water separator promotes through the second pump and is connected to ozone and H2O2 unite oxidation unit, ozone and H2O2 unite oxidation unit and connect walnut shell filter.

Description

A kind of Coal Chemical Industry spent lye pollutes complex control system
Technical field
The utility model is related to industrial waste water treatment, and more particularly to a kind of Coal Chemical Industry spent lye pollution is comprehensive Control system.
Background technology
At present olefin hydrocarbon making by coal isolation of purified process, generally removes the CO in product gas using alkali wash2、H2The sour gas such as S Body.Effective alkali (referring mainly to NaOH) concentration in its circulation alkali liquor is constantly reduced, and is the reactivity for ensureing alkali wash water, is needed not Break and supplement fresh soda in highly basic section, while discharging alkali lye, i.e. alkali-washing waste liquid from weak base section.
Spent lye is that a kind of pollutant component is complicated, the special industrial waste water that pollution concentration is high.Due under the conditions of alkali lye, Unsaturated hydrocarbons in unstripped gas can be polymerized, and sticky liquid is produced in alkali lye and is gathered in system, and connect with air Thixotroping yellowly, commonly referred to " butter ".The generation of " butter " not only results in the blocking of tower tray, pipeline and equipment, affects system Operation, and spent lye discharge can also water supply system bring severe contamination.
At present, it is domestic to solve high oil-containing spent lye pollution problem, it is generally directed to the high water quality of spent lye oil content special Point, the method for the process that custom is taken, such as burning method, oxidizing process, neutralization-combustion method.But, these methods have it to limit to Property:
1st, burning disposal is carried out to spent lye using burning method, disposable apparatus investment, day-to-day operation and administration fee compared with Height, and the tail gas for producing that burns contains a large amount of SO2、H2The pernicious gases such as S, easily cause secondary pollution, and enterprise is typically less to adopt Receive.
2nd, using the oily substance in oxidizing process degraded the spent lye, (operation temperature 190 typically based on wet oxidation process DEG C, operating pressure 3.0MPa), equipment investment and operational management require it is higher, and due in spent lye oily substance be mainly alkene The crosslinking organic matter that hydro carbons, aromatic hydrocarbons are formed, wet oxidation process is limited to the degradation efficiency of this type organic, and the method is by portion Big moulded coal enterprise is divided to use, but treatment effect is general.
3rd, using sour neutralisation, with acid neutralization spent lye pH to 6~7, subsequently into flare system, (part ethene enterprise uses The CO of sulfuric acid or glycol unit2Solution makees neutralization acid with water), but the SO produced after burning2Still result in the secondary dirt of environment Dye, and the sour dosage that neutralization is used is larger, operating cost is higher.
It is desirable to there is a kind of Coal Chemical Industry spent lye pollution complex control system effectively to solve above-mentioned prior art Defect.
Utility model content
The purpose of this utility model is to provide a kind of Coal Chemical Industry spent lye pollution complex control system to overcome existing skill The problems referred to above present in art.
For achieving the above object, the utility model provides a kind of Coal Chemical Industry spent lye pollution complex control system, the coal Chemical waste alkaline liquor pollution complex control system includes:Spent lye recovering and purifying system and spent lye reutilization system, the salkali waste Liquid recovering and purifying system includes:Wastewater collecting basin, gravity separator, profit collecting pit, air-floating apparatus, oil water separator, ozone And H2O2Co-oxidation device, walnut shell filter;The wastewater collecting basin is connected to the gravity point by the lifting of the first pump From device, the gravity separator connects the air-floating apparatus, and the gravity separator also Jing overflow launders connect the profit Collecting pit, the air-floating apparatus are connected to the oil water separator, and the pumps of oil water separator Jing second lifting is connected to described Ozone and H2O2Co-oxidation device, the ozone and H2O2Co-oxidation device connects the walnut shell filter.
Preferably, the gravity separator pressure inlets and oil water separator pressure inlets are respectively provided with H2O2Drug feeding pipeline Blender.
Preferably, the spent lye reutilization system includes:Coal gasification buck removes hardness spent lye reutilization system, coal gas Ashing water ammonia still process spent lye reutilization system and coal gasification wastewater biochemical treatment spent lye reutilization system.
Preferably, the coal gasification buck removes hardness spent lye reutilization system includes first order reaction pond and combined type except hard Device, the first order reaction pond is connected to the combined type hardness removing device by the 3rd pump;The coal gasification buck is useless except hardness Alkali lye reutilization system is used for gasification system flash evaporation unit and discharges high rigidity buck, removes in buck because of calcium ions and magnesium ions formation Permanent hardness, except the buck after hard reuse to gasification system, can reduce the increment of circulatory system fresh water again, while drop The low system-wide grey water hardness, solves equipment, pipeline scale blockage problem.
Preferably, the coal gasification buck ammonia still process spent lye reutilization system includes waste water homogeneous pond and ammonia steaming device, institute State waste water homogeneous pond and the ammonia steaming device is connected to by the 4th pump, the ammonia steaming device tower reactor waste liquid flow to sewage disposal list Unit, 10-15% ammoniacal liquor flow to sulfur recovery unit or flue gas desulfurization device in the ammonia steaming device;When gasification system discharges buck NH3It is equipment investment and the operating cost for reducing buck biochemical treatment during-N > 500mg/L, high-ammonia wastewater need to be carried out at materialization Reason removes ammonia nitrogen (processing method:Ammonia still process/stripping), in pH, treatment effeciency is optimal under 10~11 operating mode, and surplus alkalinity can fill Divide the pH for presetting gasification ash water, reduce the usage amount of fresh alkali lye, reduce operating cost, what ammonia still process/stripping device was produced 10~15% ammoniacal liquor can also deliver to the sulfur recovery unit of gasification system or flue gas desulfurization device is recycled.
Preferably, the coal gasification wastewater biochemical treatment spent lye reutilization system includes:Hydrolysis acidification pool, anaerobic reaction Device and efficient denitrification biochemistry pool;When gasification system discharges buck NH3During-N < 500mg/L, high ammonia buck need to efficiently be given birth to Thing denitrogenation processing, its mechanism is the continuous circulation of nitrification/anti-nitration reaction, and is disappeared in a large number along with comprehensive basicity in buck Consumption, is the stable operation for maintaining high-efficiency biological denitrification system, and system need to supplement a large amount of basicity, and reclaiming surplus alkalinity can be sufficiently used for Herein, the magnitude of recruitment of fresh alkali lye is reduced, operating cost is reduced.
The utility model provides a kind of Coal Chemical Industry spent lye and pollutes complex control system, the Coal Chemical Industry spent lye pollution The CO that complex control system is discharged using production technology device2Waste gas carries out breakdown of emulsion to spent lye, at the same using efficiently separating, oxygen The purifiers such as change, filtration remove oily substance and hardly degraded organic substance in spent lye, reclaim residue Na2CO3Basicity meets system System is recycled and required, reaches the purpose of the treatment of wastes with processes of wastes against one another, clean manufacturing, high concentration oily pollution has both been solved the problems, such as, while oil recovery Divide with basicity and be used in process system.
Description of the drawings
Fig. 1 is used for coal gasification buck except the Coal Chemical Industry spent lye of hardness is reclaimed and cleaning system and spent lye reutilization system Schematic flow sheet.
Fig. 2 is used for the Coal Chemical Industry spent lye of coal gasification buck ammonia still process and reclaims and cleaning system and spent lye reutilization system Schematic flow sheet.
Fig. 3 is used for the Coal Chemical Industry spent lye of coal gasification wastewater biochemical treatment and reclaims and cleaning system and spent lye recycling system The schematic flow sheet of system.
Specific embodiment
Purpose, technical scheme and advantage to implement the utility model is clearer, below in conjunction with the utility model Accompanying drawing in embodiment, is further described in more detail to the technical scheme in the utility model embodiment.In the accompanying drawings, ad initio Same or similar element is represented to end with same or similar label or the element with same or like function.Described Embodiment is a part of embodiment of the utility model, rather than the embodiment of whole.Below with reference to the enforcement of Description of Drawings Example is exemplary, it is intended to for explaining the utility model, and it is not intended that to restriction of the present utility model.Based on this practicality Embodiment in new, the every other reality that those of ordinary skill in the art are obtained under the premise of creative work is not made Example is applied, the scope of the utility model protection is belonged to.Embodiment of the present utility model is described in detail below in conjunction with the accompanying drawings.
In description of the present utility model, it is to be understood that term " " center ", " longitudinal direction ", " horizontal ", "front", "rear", The orientation or position relationship of the instruction such as "left", "right", " vertical ", " level ", " top ", " bottom " " interior ", " outward " is based on accompanying drawing institute The orientation for showing or position relationship, are for only for ease of description the utility model and simplify description, rather than indicate or imply indication Device or element must have specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to this practicality The restriction of novel protected scope.
In the broad embodiment of the utility model one, Coal Chemical Industry spent lye pollution complex control system, the Coal Chemical Industry is given up Alkali lye pollution complex control system includes:Spent lye recovering and purifying system and spent lye reutilization system, the spent lye is reclaimed Cleaning system includes:Wastewater collecting basin, gravity separator, profit collecting pit, air-floating apparatus, oil water separator, ozone and H2O2Connection Close oxidation unit, walnut shell filter;The wastewater collecting basin is connected to the gravity separator, institute by the lifting of the first pump State gravity separator and connect the air-floating apparatus, and the gravity separator also Jing overflow launders connect the profit collecting pit, The air-floating apparatus are connected to the oil water separator, the pumps of oil water separator Jing second lifted be connected to the ozone and H2O2Co-oxidation device, the ozone and H2O2Co-oxidation device connects the walnut shell filter.
As shown in figure 1, embodiment 1:With disposal ability 5m3/ h, total oil concentration 600ppm, NaOH mass concentration 4%, Na2CO3Mass concentration 4%, pH is 14 Coal Chemical Industry salkali waste liquid treating system, and purification spent lye is removed for coal gasification buck As a example by hardness system, first with the CO of production technology device discharge2Waste gas is in wastewater collecting basin 1 to oil-containing olefin hydrocarbon making by coal salkali waste Liquid carries out breakdown of emulsion, processes 5m3/ h spent lyes, need the CO of 600-800kg/h2Waste gas;Spent lye is promoted to Gravity Separation after breakdown of emulsion Device 2 carries out water-oil separating, and wherein Jing after overflow launder collection from profit collecting pit is flow to, spent lye flow to air-floating apparatus 3 to oil slick certainly; Meanwhile, the pressure inlets of gravity separator 2 arrange H2O2Drug feeding pipeline blender, using the time of staying oxidation section of gravity separator 2 Divide dissolubility oily substance (olefin compound).Demulsifier, flocculant are added in the water distribution mixing channel of air-floating apparatus 3, device is floated on The oily substance Jing air supporting mud scrapers on surface are collected to scum trough, and the spent lye Jing collector pipes in air-floating apparatus are collected to air supporting Pond.The water outlet Jing pumps of air-floating apparatus 3 are promoted to oil water separator 4, and by high density filter core dispersed oil, oil water separator 4 are retained Inside is provided with oil collecting zone, and the oils of collection flow to profit collecting pit by pressure, and spent lye Jing pressure flow to intermediate pool, profit The pressure inlets of separator 4 arrange H2O2Drug feeding pipeline blender, is aoxidized using the time of staying of oil water separator 4 and intermediate pool Partial solubility oily substance (olefin compound).Intermediate pool waste water Jing pumps are promoted to ozone and H2O2Co-oxidation breakdown of emulsion is filled 5 are put, by combining the dissolubility oily substance (aromatic hydrocarbon substance) that Strong oxdiative is degraded in spent lye.Co-oxidation breaking device 5 Discharge pressure flow to walnut shell filter 6, further removes the remaining various oily substances of spent lye, it is ensured that reclaims spent lye and contains Oil mass is down to below 40mg/L, reaches system and recycles requirement.The oil in spent lye is removed Jing after two-stage is separated, aoxidized, filtering Class material, water outlet oil content is down to 40ppm, Na2CO3Content about 9.3%.
Reclaim oils method of disposal:Reclaim oil quality about 66kg/d, Jing oil slick storage tank collect after periodically deliver to coal bunker with Gasification furnace is sent to burn after coal slurry mixing.
The method that spent lye is recycled:Reclaim Na2CO3Quality about 11.16t/d, the alkali lye after purification is delivered to anti-including one-level Answering the gasification ash water clarifier of pond 7 and combined type hardness removing device 8 carries out buck except hardness is (mainly for permanent hard in buck Degree), the grey water hardness is down to into below 200ppm by 2000ppm, except the buck after hard, to be back to the gasification ash water circulatory system sharp again With so as to reduce the increment of technique fresh water.
As shown in Fig. 2 embodiment 2:With disposal ability 5m3/ h, total oil concentration 600ppm, NaOH mass concentration 4%, Na2CO3Mass concentration 4%, pH is 14 Coal Chemical Industry salkali waste liquid treating system, and purification spent lye is for the steaming of coal gasification buck As a example by ammonia system, first with the CO of production technology device discharge2Waste gas is in wastewater collecting basin 1 to oil-containing olefin hydrocarbon making by coal spent lye Breakdown of emulsion is carried out, 5m is processed3/ h spent lyes, need the CO of 600-800kg/h2Waste gas;Spent lye is promoted to gravity separator after breakdown of emulsion 2 carry out water-oil separating, and wherein Jing after overflow launder collection from profit collecting pit is flow to, spent lye flow to air-floating apparatus 3 to oil slick certainly;Together When, the pressure inlets of gravity separator 2 arrange H2O2Drug feeding pipeline blender, using the time of staying oxidized portion of gravity separator 2 Dissolubility oily substance (olefin compound).Demulsifier, flocculant are added in the water distribution mixing channel of air-floating apparatus 3, device table is floated on The oily substance Jing air supporting mud scrapers in face are collected to scum trough, and the spent lye Jing collector pipes in air-floating apparatus are collected to air supporting water outlet Pond.The water outlet Jing pumps of air-floating apparatus 3 are promoted to oil water separator 4, dispersed oil are retained by high density filter core, in oil water separator 4 Portion is provided with oil collecting zone, and the oils of collection flow to profit collecting pit by pressure, and spent lye Jing pressure flow to intermediate pool, profit point From the pressure inlets of device 4, H is set2O2Drug feeding pipeline blender, using oil water separator 4 and the time of staying oxidation section of intermediate pool Divide dissolubility oily substance (olefin compound).Intermediate pool waste water Jing pumps are promoted to ozone and H2O2Co-oxidation breaking device 5, by combining the dissolubility oily substance (aromatic hydrocarbon substance) that Strong oxdiative is degraded in spent lye.Co-oxidation breaking device 5 goes out Water pressure flow to walnut shell filter 6, further removes the remaining various oily substances of spent lye, it is ensured that reclaim spent lye oil-containing Amount is down to below 40mg/L, reaches system and recycles requirement.The oils in spent lye is removed Jing after two-stage is separated, aoxidized, filtering Material, water outlet oil content is down to 40ppm, Na2CO3Content about 9.3%.
Reclaim oils method of disposal:Reclaim oil quality about 66kg/d, Jing oil slick storage tank collect after periodically deliver to coal bunker with Gasification furnace is sent to burn after coal slurry mixing.
The method for recycling alkali lye basicity:When gasification system discharges buck NH3It is to reduce coal gas during-N > 500mg/L The equipment investment of change system biochemical wastewater treatment and operating cost, high-ammonia wastewater passes sequentially through waste water homogeneous pond 7 and ammonia steaming device 8 Ammonia still process/stripping process is carried out to high-ammonia wastewater except ammonia nitrogen, is the optimization process operating mode for ensureing buck pH between 10-11, reclaim alkali Degree can be used for the pH of presetting gasification ash water, reduce the usage amount of fresh alkali lye, reduce operating cost, and ammonia still process/stripping device is produced 10-15% ammoniacal liquor can also deliver to gasification system sulfur recovery unit or flue gas desulfurization device recycle.
As shown in figure 3, embodiment 3 is with disposal ability 5m3/ h, total oil concentration 600ppm, NaOH mass concentration 4%, Na2CO3 Mass concentration 4%, pH is 14 Coal Chemical Industry salkali waste liquid treating system, and purification spent lye is used for coal gasification wastewater biochemical treatment As a example by system, first with the CO of production technology device discharge2Waste gas enters in wastewater collecting basin 1 to oil-containing olefin hydrocarbon making by coal spent lye Row breakdown of emulsion, processes 5m3/ h spent lyes, need the CO of 600-800kg/h2Waste gas;Spent lye is promoted to gravity separator 2 after breakdown of emulsion Water-oil separating is carried out, wherein Jing after overflow launder collection from profit collecting pit is flow to, spent lye flow to air-floating apparatus 3 to oil slick certainly;Together When, the pressure inlets of gravity separator 2 arrange H2O2Drug feeding pipeline blender, using the time of staying oxidized portion of gravity separator 2 Dissolubility oily substance (olefin compound).Demulsifier, flocculant are added in the water distribution mixing channel of air-floating apparatus 3, device table is floated on The oily substance Jing air supporting mud scrapers in face are collected to scum trough, and the spent lye Jing collector pipes in air-floating apparatus are collected to air supporting water outlet Pond.The water outlet Jing pumps of air-floating apparatus 3 are promoted to oil water separator 4, dispersed oil are retained by high density filter core, in oil water separator 4 Portion is provided with oil collecting zone, and the oils of collection flow to profit collecting pit by pressure, and spent lye Jing pressure flow to intermediate pool, profit point From the pressure inlets of device 4, H is set2O2Drug feeding pipeline blender, using oil water separator 4 and the time of staying oxidation section of intermediate pool Divide dissolubility oily substance (olefin compound).Intermediate pool waste water Jing pumps are promoted to ozone and H2O2Co-oxidation breaking device 5, by combining the dissolubility oily substance (aromatic hydrocarbon substance) that Strong oxdiative is degraded in spent lye.Co-oxidation breaking device 5 goes out Water pressure flow to walnut shell filter 6, further removes the remaining various oily substances of spent lye, it is ensured that reclaim spent lye oil-containing Amount is down to below 40mg/L, reaches system and recycles requirement.The oils in spent lye is removed Jing after two-stage is separated, aoxidized, filtering Material, water outlet oil content is down to 40ppm, Na2CO3Content about 9.3%.
Reclaim oils method of disposal:Reclaim oil quality about 66kg/d, Jing oil slick storage tank collect after periodically deliver to coal bunker with Gasification furnace is sent to burn after coal slurry mixing.
The method for recycling alkali lye basicity:When gasification system discharge buck NH3-N < 500mg/L when, buck still need into The process of row biological denitrificaion, with nitrification/denitrification process, comprehensive basicity is consumed in a large number in buck, is to maintain high-efficiency biological denitrification The stable operation of system, hydrolysis acidification pool 7, anaerobic reactor 8 and efficient denitrification biochemical treatment 9 all need to supplement a large amount of basicity, return Receiving surplus alkalinity ground utilization can reduce the magnitude of recruitment of fresh alkali lye, reduce operating cost.
It is last it is to be noted that:Above example is only illustrating the technical solution of the utility model, rather than it is limited System.Although being described in detail to the utility model with reference to the foregoing embodiments, one of ordinary skill in the art should manage Solution:It still can modify to the technical scheme described in foregoing embodiments, or which part technical characteristic is entered Row equivalent;And these modifications or replacement, do not make each embodiment of essence disengaging the utility model of appropriate technical solution The spirit and scope of technical scheme.

Claims (6)

1. a kind of Coal Chemical Industry spent lye pollutes complex control system, it is characterised in that include:Spent lye recovering and purifying system and useless Alkali lye reutilization system, the spent lye recovering and purifying system includes:Wastewater collecting basin, gravity separator, profit collecting pit, gas Floating device, oil water separator, ozone and H2O2 co-oxidation devices, walnut shell filter;The wastewater collecting basin passes through first The lifting of pump is connected to the gravity separator, and the gravity separator connects the air-floating apparatus, and the Gravity Separation Device also Jing overflow launders connect the profit collecting pit, and the air-floating apparatus are connected to the oil water separator, the water-oil separating The pumps of device Jing second are lifted and are connected to the ozone and H2O2 co-oxidation devices, and the ozone and H2O2 co-oxidations device connect The walnut shell filter.
2. Coal Chemical Industry spent lye according to claim 1 pollutes complex control system, it is characterised in that:The Gravity Separation Device pressure inlets and oil water separator pressure inlets are respectively provided with H2O2 drug feeding pipeline blenders.
3. Coal Chemical Industry spent lye according to claim 1 pollutes complex control system, it is characterised in that:The spent lye is again Included using system:Coal gasification buck removes hardness spent lye reutilization system, coal gasification buck ammonia still process spent lye reutilization system With coal gasification wastewater biochemical treatment spent lye reutilization system.
4. Coal Chemical Industry spent lye according to claim 3 pollutes complex control system, it is characterised in that:The coal gas ashing Water includes first order reaction pond and combined type hardness removing device except hardness spent lye reutilization system, and the first order reaction pond passes through the 3rd Pump is connected to the combined type hardness removing device;The coal gasification buck is used for gasification system except hardness spent lye reutilization system Flash evaporation unit discharges high rigidity buck, removes the permanent hardness formed because of calcium ions and magnesium ions in buck.
5. Coal Chemical Industry spent lye according to claim 3 pollutes complex control system, it is characterised in that:The coal gas ashing Water ammonia still process spent lye reutilization system includes waste water homogeneous pond and ammonia steaming device, and the waste water homogeneous pond is connected to by the 4th pump The ammonia steaming device, the ammonia steaming device tower reactor waste liquid flow to sewage treatment unit, 10-15% ammoniacal liquor in the ammonia steaming device It flow to sulfur recovery unit or flue gas desulfurization device.
6. Coal Chemical Industry spent lye according to claim 3 pollutes complex control system, it is characterised in that:The coal gasification is dirty Water biochemical treatment spent lye reutilization system includes:Hydrolysis acidification pool, anaerobic reactor and efficient denitrification biochemistry pool.
CN201620756939.5U 2016-07-18 2016-07-18 Coal industry waste lye pollutes integrated control system Active CN206156893U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106007098A (en) * 2016-07-18 2016-10-12 蒲城清洁能源化工有限责任公司 Integrated control system for waste alkaline liquid pollution in coal chemical industry
CN108191594A (en) * 2017-11-10 2018-06-22 中国天辰工程有限公司 A kind of preprocess method of MTO devices spent lye

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106007098A (en) * 2016-07-18 2016-10-12 蒲城清洁能源化工有限责任公司 Integrated control system for waste alkaline liquid pollution in coal chemical industry
CN108191594A (en) * 2017-11-10 2018-06-22 中国天辰工程有限公司 A kind of preprocess method of MTO devices spent lye

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