CN108892353A - Oil field mining liquid central treating station process for treating oil-containing sludge and device - Google Patents
Oil field mining liquid central treating station process for treating oil-containing sludge and device Download PDFInfo
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- CN108892353A CN108892353A CN201811095451.2A CN201811095451A CN108892353A CN 108892353 A CN108892353 A CN 108892353A CN 201811095451 A CN201811095451 A CN 201811095451A CN 108892353 A CN108892353 A CN 108892353A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/06—Sludge reduction, e.g. by lysis
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- Treatment Of Sludge (AREA)
Abstract
The present invention relates to technical fields at oil field mining liquid oily sludge, it is a kind of oil field mining liquid central treating station process for treating oil-containing sludge and device, the oil field mining liquid central treating station process for treating oil-containing sludge, by the way that the sludge isolated in oil field mining liquid is washed by heat chemistry, sludge chemical combined biological prosthetic and up to standard carries out these three stages of resource utilization, realize oil field mining liquid central treating station oily sludge harmless treatment utilization, simultaneously, recycle-water after centrifugation is also used as washing water circulation use, reduce sewage discharge, its resource is set to be utilized to the greatest extent, with significant environmental benefit, Social benefit and economic benefit.The present invention need to only add oily sludge heat chemistry washing oil removing pot and sludge prosthetic device on the original device of oil field mining liquid central treating station, and simple process, operation is easy to operate, and equipment cost is low, meets the idea of development of environmental protection and the utilization of resources.
Description
Technical field
It is that a kind of oil field mining liquid central treating station contains the present invention relates to oil field mining liquid contained Mud Treatment Technology field
Greasy dirt processing method and processing device.
Background technique
Oil field mining liquid central treating station oily sludge refers to is deposited on various storages during oil field mining liquid collection is defeated
Tank（Crude Treatment system, sewage disposal system）A kind of oily solid sludge of bottom.Currently, in entering with most oilfields
Later period mining phase, the oily sludge that oil field mining liquid central treating station generates are growing day by day.Oily sludge ingredient is extremely complex,
It is mainly made of oil emulsion, water, solid suspension and various chemical agents etc., the salt content of oily sludge is very high（Sewage mine
Change degree is 8 × 104Mg/L to 14 × 104mg/L）, oil content accounts for the 10% to 20% of dewatered sludge, and viscosity is big, and mud granule is superfine, is
The hydroaropic substance of colloid form structure, the settleability and filterability of sludge are poor, and dehydration difficulty is very big.In addition, also containing in greasy dirt
There is the noxious material of the stenches such as a certain amount of benzene homologues, phenols, anthracene, pyrene.
With industrial rapid development, environmental pollution is got worse.And people to the protection of living environment and change
Good will, which is known, constantly to be reinforced, and the relevant laws and regulations of environmental protection also have stringent regulation to the discharge standard of oily sludge.Root
The new pollution emission standard formulated according to national four ministries and commissions joint：Untreated oily sludge discharge charging standard is 1000 yuan/ton, this
The production cost of enterprise will be greatly increased.Oily sludge has been put into《National Hazard waste catalogue》In oily waste water species,《State
Family's promotion law on cleaner production》It is required that innoxious and recycling treatment must be carried out to oily sludge.
The processing standard of oily sludge, is generally determined by the whereabouts after Treatment of Sludge, at domestic and international most important terminal
The mode of setting is landfill and builds the road that, to avoid generating adverse effect to soil, various countries provide the index of oil content, in state
On border, due to the difference in geology and geographical conditions, soil is different to the tolerance degree of oils organic matter for various regions, therefore for
TPH in sludge（Total petroleum hydrocarbon）Or oil content, ununified standard in the world, but many countries and regions all bases
The actual conditions of this area propose the corresponding dedicated index in scene in the form of regulation or instructional criterion.The U.S., France add and take
Great Deng state regulation oily sludge oil content, for filling, is used to build the road less than 5% less than 2%.Oily sludge is classified as danger by China
Dangerous solid waste, but quantizating index is not proposed to the oil content in oily sludge, only in GB4284-84《It is dirty in agricultural sludge
Contaminate the standard of object control》And GB/T23486-2009《Urban sewage treatment plant sludge disposes afforestation shale》In, to agriculture
It is provided with sludge and afforestation with the mineral oil content in mud, it is desirable that highest permissible level≤3000mg/kg（0.3%）.
On 2 16th, 2011 publication HJ607-2011 of Environmental Protection Department《Waste mineral oil recycles pollution control technology specification》, 2011
On July 1, in implements, it is specified that 5% oily sludge of oil content >, oil-sand should carry out regeneration, and oil content is answered small after greasy filth sand separation
In 2%.
Domestic each main oilfield strengthens contained Mud Treatment Technology research, and the research departments such as each universities and colleges also assist in
Wherein, a variety of process for treating oil-containing sludge and technique have been developed at present, such as：Incineration method, extraction, bioanalysis etc., but because of place
Reason cost requires the factors such as process conditions to limit, and the practical application in industry of institute's research achievement is few, and domestic majority oil field still uses
Landfill method handles oily sludge, and it is serious to fill phenomenon not up to standard；A small number of oil fields are separated by solid-liquid separation using hypergravity, ultrasonic wave penetrates processing
The methods of recycling crude oil, but oily sludge oil content meet the requirement of environmental protection not yet after handling.Therefore, establishing one kind being capable of General Office
Reason and the method for utilizing oily sludge, fundamentally solving oily sludge is that domestic each oil field is urgent to the technology of the pollution of environment
Problem to be solved.
Summary of the invention
The present invention provides a kind of oil field mining liquid central treating station process for treating oil-containing sludge and devices, overcome above-mentioned
The deficiency of the prior art can effectively solve existing disposal of oily sludge presence and fill oily sludge oil-containing after not up to standard, processing
The problem that amount is high and processing is difficult.
Technical solution of the present invention first is that being realized by following measures：A kind of oil field mining liquid central treating station contains
Greasy dirt processing method carries out by the following method：The first step, oil field mining liquid after crude oil treating device removes sewage,
The first obtained oily sludge is sent to oily sludge concentration basin, wherein the sewage of removing passes through at the recycling of sewage-treatment plant
The second oily sludge obtained after reason is sent to oily sludge concentration basin, the first oily sludge and the second oily sludge containing greasy dirt
Gravity settling separation is carried out in mud thickener, obtains thickening sludge；Second step, thickening sludge are sent into the washing of oily sludge heat chemistry
It is added and washes on feed-line in oil removing pot, and between oily sludge concentration basin and oily sludge heat chemistry washing oil removing pot
Medicament, steam and washing water obtain upper layer oil slick and lower layer after the Hybrid Heating washing of washing medicament, steam and washing water
Wash sludge；Third step, upper layer floating oil collecting enter oil slick storage tank, and sludge washs in the centrifugation that joined sludge dehydrating agent in lower layer
Centrifugation outlet sewage and desiccation oily sludge are obtained in machine after being centrifuged, wherein centrifugation outlet sewage recycling is slow into recycle-water
It rushes in tank, as the washing water in oily sludge heat chemistry washing oil removing pot；4th step, desiccation oily sludge enter sludge reparation
Sludge renovation agent is added into desiccation oily sludge for device, and desiccation oily sludge and sludge renovation agent are in sludge prosthetic device
Chemical combined biological prosthetic reaction occurs, the sludge up to standard reacted drains into sludge storage up to standard field；5th step, sludge up to standard
Store field in sludge up to standard after innoxious, recycling treatment, as oil field pad well site, roadbed, water quality purification material with
And afforestation mud.
Here is further optimization or/and improvement of one of the above technical solutions of the invention：
The oil content of above-mentioned desiccation oily sludge is less than 2%, and the oil content of sludge up to standard is less than 0.3%.
Above-mentioned washing medicament is the substance or alkaloids after alkaloids are compounded with surfactant substance.
Above-mentioned alkaloids are one of sodium hydroxide, sodium carbonate, sodium phosphate, sodium tripolyphosphate and sodium metasilicate, and table is living
Agent substance is one of polyethers, neopelex and polysorbate.
Object after above-mentioned sludge renovation agent is oxidants substance, B substance, oxidants substance are compounded with B substance
One of matter, sludge dehydrating agent are polyacrylamide, wherein B substance is biological inoculum and its metabolite.
Above-mentioned oxidants substance is one of ammonium persulfate, sodium peroxydisulfate, potassium peroxydisulfate and sodium hypochlorite, biological bacteria
Kind is one of rhamnolipid and efficient hydrocarbon oxidation bacteria.
In above-mentioned second step, Hybrid Heating wash temperature is 30 DEG C to 90 DEG C, and the additional amount of washing water is thickening sludge weight
2 times of amount；In 4th step, the additional amount of sludge renovation agent is the 1% to 3% of desiccation oily sludge weight.
Technical solution of the present invention second is that being realized by following measures：It is a kind of to implement above-mentioned oil field mining liquid concentration
The device for the treatment of stations process for treating oil-containing sludge, including the washing of crude oil treating device, sewage-treatment plant, oily sludge heat chemistry
Oil removing pot, centrifuge and sludge prosthetic device, it is fixed between crude oil treating device water outlet and sewage-treatment plant water inlet to connect
It is connected with sewage pipeline, fixation is communicated with the first sludge pipe between crude oil treating device mud mouth and oily sludge concentration basin mud inlet
Line is communicated with sludge discharge pipeline, oily sludge concentration basin mud extraction between sewage-treatment plant mud mouth and the first oily sludge pipeline
Fixation is communicated with the second sludge pipeline, the second oily sludge pipeline between mouth and oily sludge heat chemistry washing oil removing pot mud inlet
On be sequentially communicated steam pipe line and washing medicament pipeline, oily sludge heat chemistry washes oil removing pot mud mouth and centrifuge into mud
Fixation is communicated with third sludge pipeline between mouthful, fixed between centrifuge mud mouth and sludge prosthetic device mud inlet to be communicated with the
Four sludge pipelines.
Here is further optimization or/and improvement of the technical scheme ii of the invention：
Above-mentioned further includes that oil slick storage tank, recycle-water surge tank and sludge up to standard storage field, oily sludge heat chemistry wash oil removing pot
Fixed between oil outlet and oil slick storage tank oil inlet to be communicated with oil slick pipeline, sludge prosthetic device mud mouth and sludge up to standard store
Fixation is communicated with the 5th sludge pipeline between the mud inlet of field, fixed between centrifuge water outlet and recycle-water surge tank water inlet to connect
It is connected with recycle-water pipeline, the second sludge pipe between recycle-water surge tank water outlet and steam pipe line outlet and washing agent outlet
Washing water pipeline is communicated on line.
Above-mentioned third is communicated with sludge renovation agent on the 4th sludge pipeline containing sludge dehydrating agent pipeline is communicated on oil pipeline
Pipeline.
The present invention need to only add the washing of oily sludge heat chemistry on the original device of oil field mining liquid central treating station and remove
Oil tank and sludge prosthetic device, simple process runs easy to operate, and equipment cost is low, meets environmental protection and the utilization of resources
Idea of development.
Detailed description of the invention
Attached drawing 1 is the process structure schematic diagram of preferred embodiment 8.
Coding in attached drawing 1 is respectively：1 is crude oil treating device, and 2 be sewage-treatment plant, and 3 are concentrated for oily sludge
Pond, 4 wash oil removing pot for oily sludge heat chemistry, and 5 be centrifuge, and 6 be sludge prosthetic device, and 7 be oil slick storage tank, and 8 be recycling
Water surge tank, 9 store field for sludge up to standard, and 10 be sewage pipeline, and 11 be the first sludge pipeline, and 12 be sludge discharge pipeline, and 13 be the
Two sludge pipelines, 14 be third sludge pipeline, and 15 be the 4th sludge pipeline, and 16 be the 5th sludge pipeline, and 17 be steam pipe line, 18
To wash medicament pipeline, 19 be recycle-water pipeline, and 20 be washing water pipeline, and 21 be oil slick pipeline, and 22 be sludge dehydrating agent pipeline,
23 be sludge renovation agent pipeline.
Specific embodiment
The present invention is not limited by the following examples, can determine according to the technique and scheme of the present invention with actual conditions specific
Embodiment.It is previously mentioned various chemical reagent and chemical article in the present invention unless otherwise specified, is public in the prior art
Know common chemical reagent and chemical article；Percentage in the present invention does not have specified otherwise such as, is mass percent；This hair
It is the aqueous solution that solvent is water, for example, hydrochloric acid solution is aqueous hydrochloric acid solution if the solution in bright is without specified otherwise；This
Room temperature, room temperature in invention refer generally to 15 DEG C to 25 DEG C of temperature, are commonly defined as 25 DEG C.
The present invention will be further described below with reference to examples：
Embodiment 1：The oil field mining liquid central treating station process for treating oil-containing sludge, carries out by the following method：The first step, oil
After crude oil treating device removes sewage, the first obtained oily sludge is sent to oily sludge concentration basin 3 field Produced Liquid,
In, the second oily sludge that the sewage of removing obtains after the recovery processing of sewage-treatment plant 2 send to oily sludge and is concentrated
Pond 3, the first oily sludge and the second oily sludge carry out gravity settling separation in oily sludge concentration basin 3, and it is dirty to obtain thickening
Mud；Second step, thickening sludge are sent into oily sludge heat chemistry washing oil removing pot 4, and in oily sludge concentration basin 3 and contain greasy dirt
Mud heat chemistry, which is washed on the feed-line between oil removing pot 4, is added washing medicament, steam and washing water, in washing medicament, steam
After the Hybrid Heating washing of washing water, upper layer oil slick and lower layer's washing sludge are obtained；Third step, upper layer floating oil collecting enter floating
Oil tank 7, lower layer's washing sludge obtain centrifugation outlet sewage in the centrifuge 5 that joined sludge dehydrating agent and are done after being centrifuged
Change oily sludge, wherein centrifugation outlet sewage recycling enters in recycle-water surge tank 8, removes as the washing of oily sludge heat chemistry
Washing water in oil tank 4；4th step, desiccation oily sludge enter sludge prosthetic device 6, and sludge is added into desiccation oily sludge
Renovation agent, desiccation oily sludge occur in sludge prosthetic device 6 with sludge renovation agent it is chemical combined it is biological prosthetic react, react
Obtained sludge up to standard drains into sludge storage up to standard field 9；5th step, sludge up to standard store the sludge up to standard in field 9 by harmless
Change, after recycling treatment, as oil field pad well site, roadbed, water quality purification material and afforestation mud.
Oil field mining liquid central treating station of the present invention process for treating oil-containing sludge is contained by oil field mining liquid central treating station
The innoxious treatment process with recycling of greasy dirt, first stage are washed by heat chemistry and are down to oily sludge desiccation oil content
2%, second stage using it is chemical combined it is biological prosthetic reaction by sludge drying oil content be down to 0.3% hereinafter, the phase III be by
Sludge up to standard carries out resource utilization, is mainly used as pad well site, roadbed, water quality purification material and afforestation soil etc., thus
It realizes that its resource can be utilized to the greatest extent, there is significant environmental benefit, Social benefit and economic benefit.At crude oil
Reason device is the existing equipment for being widely known for oil field mining liquid central treating station crude Treatment.
Embodiment 2：As the optimization of above-described embodiment, less than 2%, sludge up to standard contains the oil content of desiccation oily sludge
Oil cut rate is less than 0.3%.
Embodiment 3：As the optimization of above-described embodiment, washing medicament is that alkaloids are compounded with surfactant substance
Substance or alkaloids afterwards.
In the present invention, washing medicament can separate oil therein from sludge, and the mass concentration for washing medicament is
5000mg/L to 10000mg/L.
Embodiment 4：As the optimization of above-described embodiment, alkaloids are sodium hydroxide, sodium carbonate, sodium phosphate, trimerization phosphorus
One of sour sodium and sodium metasilicate, surfactant substance are one of polyethers, neopelex and polysorbate.
Embodiment 5：As the optimization of above-described embodiment, sludge renovation agent is oxidants substance, B substance, oxidant
Substance compounded with B substance after one of substance, sludge dehydrating agent is polyacrylamide, wherein B substance is biology
Strain and its metabolite.
In the present invention, sludge renovation agent can make oil contained in sludge be degraded to carbon dioxide and water, sludge dewatering
The mass concentration of agent is 300mg/L to 400mg/L.
Embodiment 6：As the optimization of above-described embodiment, oxidants substance is ammonium persulfate, sodium peroxydisulfate, potassium peroxydisulfate
One of with sodium hypochlorite, biological inoculum is one of rhamnolipid and efficient hydrocarbon oxidation bacteria.
Embodiment 7：As the optimization of above-described embodiment, in second step, Hybrid Heating wash temperature is 30 DEG C to 90 DEG C, is washed
The additional amount for washing water is 2 times for being thickened sludge weight；In 4th step, the additional amount of sludge renovation agent is desiccation oily sludge weight
1% to 3%.
Embodiment 8：As shown in Fig. 1, oil field mining liquid central treating station oily sludge described in the implementation above-described embodiment
The device of processing method, including crude oil treating device 1, sewage-treatment plant 2, oily sludge heat chemistry washing oil removing pot 4, centrifugation
Machine 5 and sludge prosthetic device 6, fixation is communicated with sewage between 2 water inlet of 1 water outlet of crude oil treating device and sewage-treatment plant
Pipeline 10, fixation is communicated with the first sludge pipeline between 3 mud inlet of 1 mud mouth of crude oil treating device and oily sludge concentration basin
11, sludge discharge pipeline 12 is communicated between 2 mud mouth of sewage-treatment plant and the first sludge pipeline 11, oily sludge concentration basin 3 goes out
Fixation is communicated with the second sludge pipeline 13, the second sludge pipe between mud mouth and oily sludge heat chemistry washing 4 mud inlet of oil removing pot
Be sequentially communicated on line 13 steam pipe line 17 and washing medicament pipeline 18, oily sludge heat chemistry wash 4 mud mouth of oil removing pot with
It is fixed between 5 mud inlet of centrifuge to be communicated with third sludge pipeline 14,5 mud mouth of centrifuge and 6 mud inlet of sludge prosthetic device
Between fixation be communicated with the 4th sludge pipeline 15.
Above-mentioned apparatus can be made further optimization and/or improvements according to actual needs：
It as shown in Fig. 1, further include oil slick storage tank 7, recycle-water surge tank 8 and sludge up to standard storage field 9, oily sludge heat chemistry
Fixation is communicated with oil slick pipeline 21,6 mud extraction of sludge prosthetic device between washing 4 oil outlet of oil removing pot and 7 oil inlet of oil slick storage tank
Fixed between mouth and sludge up to standard storage 9 mud inlet of field to be communicated with the 5th sludge pipeline 16,5 water outlet of centrifuge and recycle-water are slow
It rushes to fix between 8 water inlet of tank and is communicated with recycle-water pipeline 19,8 water outlet of recycle-water surge tank is exported with steam pipe line 17 and water
Washing water pipeline 20 is communicated on the second sludge pipeline 13 washed between agent outlet.
The present invention enters the water of 5 water outlet of centrifuge in recycle-water surge tank 8 buffers, and is used as incorporation oily sludge thermalization
The washing water on the second sludge pipeline 13 of washing 4 mud inlet of oil removing pot connection is learned, realizes the washing of oily sludge heat chemistry
Washing water follows bad utilization, has on the one hand saved the energy, on the other hand reduces the pollution of discharge of wastewater bring.
As shown in Fig. 1, it is communicated with sludge dehydrating agent pipeline 22 on third sludge pipeline 14, connects on the 4th sludge pipeline 15
It is connected with sludge renovation agent pipeline 23.
As needed, the oily sludge and sludge dehydrating agent pipeline 22 that oily sludge heat chemistry washing oil removing pot 4 is discharged add
The sludge dehydrating agent entered mixed in third sludge pipeline 14 after enter centrifuge 5 in, by oily sludge water and sludge from
The heart separates, and water enters recycle-water surge tank, and sludge and the sludge renovation agent being added by sludge renovation agent pipeline 23 are dirty the 4th
In mud pipeline 15 after mixing, into sludge prosthetic device 6 in carry out sludge reparation reaction, remove the heavy metal in sludge, thus
So that treated sludge is for pad well site, roadbed, water quality purification material and afforestation soil etc..
The present invention need to only add hot oily sludge heat chemistry washing on the original device of oil field mining liquid central treating station
Oil removing pot 4 and sludge prosthetic device 6, simple process, operation is easy to operate, and equipment cost is low, meets environmental protection and resource benefit
Idea of development.
The above technical features constitute embodiments of the present invention, can basis with stronger adaptability and implementation result
Actual needs increases and decreases non-essential technical characteristic, to meet the needs of different situations.
The use process of the embodiment of the present invention 8：The first step, oil field mining liquid after crude oil treating device 1 removes sewage,
The first obtained oily sludge is sent through the first sludge pipeline 11 to oily sludge concentration basin 3, wherein the sewage of removing passes through sewage
The second oily sludge that pipeline 10 enters in sewage-treatment plant 2 and obtains after being recycled, send through sludge discharge pipeline 12 to oil-containing
Sludge concentration tank 3, the first oily sludge and the second oily sludge carry out gravity settling separation in oily sludge concentration basin 3, obtain
To thickening sludge；Second step, thickening sludge are sent into oily sludge heat chemistry washing oil removing pot 4 through the second sludge pipeline 13, and
On the second sludge pipeline 13, washing medicine is separately added by steam pipe line 17, washing medicament pipeline 18 and washing water pipeline 20
Agent, steam and washing water obtain upper layer oil slick and lower layer wash after the Hybrid Heating washing of washing medicament, steam and washing water
Wash sludge；Third step, upper layer oil slick enter oil slick storage tank 7 through the collection of oil slick pipeline 21, and sludge washs de- through sludge in lower layer
Aqua pipeline 22 joined in the centrifuge 5 of sludge dehydrating agent, and centrifugation outlet sewage and desiccation oily sludge are obtained after being centrifuged,
Wherein, centrifugation outlet sewage is entered in recycle-water surge tank 8 by recycle-water pipeline 19, is removed as the washing of oily sludge heat chemistry
Washing water in oil tank 4；4th step, desiccation oily sludge enter sludge prosthetic device 6 through the 4th sludge pipeline 15, pass through sludge
Sludge renovation agent is added into desiccation oily sludge for renovation agent pipeline 23, and desiccation oily sludge and sludge renovation agent are in sludge reparation
Chemical combined biological prosthetic reaction occurs in device 6, the sludge up to standard reacted drains into sludge up to standard through the 5th pipeline 16 and deposits
Store up field 9；5th step, sludge up to standard store the sludge up to standard in field 9 after innoxious, recycling treatment, pad well as oil field
Field, roadbed, water quality purification material and afforestation mud.
Claims (10)
1. a kind of oil field mining liquid central treating station process for treating oil-containing sludge, it is characterised in that carry out by the following method：The
One step, after crude oil treating device removes sewage, the first obtained oily sludge send to oily sludge and is concentrated oil field mining liquid
Pond, wherein the second oily sludge that the sewage of removing obtains after the recovery processing of sewage-treatment plant is sent to oily sludge
Concentration basin, the first oily sludge and the second oily sludge carry out gravity settling separation in oily sludge concentration basin, are thickened
Sludge；Second step, thickening sludge are sent into oily sludge heat chemistry washing oil removing pot, and in oily sludge concentration basin and contain greasy dirt
Mud heat chemistry, which is washed on the feed-line between oil removing pot, is added washing medicament, steam and washing water, washing medicament, steam and
After the Hybrid Heating washing of washing water, upper layer oil slick and lower layer's washing sludge are obtained；Third step, upper layer floating oil collecting enter oil slick
Storage tank, lower layer's washing sludge obtains centrifugation outlet sewage after being centrifuged in the centrifuge that joined sludge dehydrating agent and desiccation contains
Greasy dirt, wherein centrifugation outlet sewage recycling enters in recycle-water surge tank, as in oily sludge heat chemistry washing oil removing pot
Washing water；4th step, desiccation oily sludge enter sludge prosthetic device, and sludge renovation agent is added into desiccation oily sludge,
Desiccation oily sludge occur in sludge prosthetic device with sludge renovation agent it is chemical combined it is biological prosthetic react, that reacts reaches
Mark sludge drains into sludge storage up to standard field；5th step, sludge up to standard store the sludge up to standard in field by innoxious, recycling
After reason, as oil field pad well site, roadbed, water quality purification material and afforestation mud.
2. oil field mining liquid central treating station according to claim 1 process for treating oil-containing sludge, it is characterised in that desiccation
The oil content of oily sludge is less than 2%, and the oil content of sludge up to standard is less than 0.3%.
3. oil field mining liquid central treating station according to claim 1 or 2 process for treating oil-containing sludge, it is characterised in that water
Wash agent is the substance or alkaloids after alkaloids are compounded with surfactant substance.
4. oil field mining liquid central treating station according to claim 3 process for treating oil-containing sludge, it is characterised in that bases
Substance is one of sodium hydroxide, sodium carbonate, sodium phosphate, sodium tripolyphosphate and sodium metasilicate, and surfactant substance is polyethers, ten
One of dialkyl benzene sulfonic acids sodium and polysorbate.
5. oil field mining liquid central treating station according to claim 1 or 2 or 3 or 4 process for treating oil-containing sludge, feature
One be in the substance after sludge renovation agent compounds for oxidants substance, B substance, oxidants substance with B substance
Kind, sludge dehydrating agent is polyacrylamide, wherein B substance is biological inoculum and its metabolite.
6. oil field mining liquid central treating station according to claim 5 process for treating oil-containing sludge, it is characterised in that oxidation
Agent substance is one of ammonium persulfate, sodium peroxydisulfate, potassium peroxydisulfate and sodium hypochlorite, and biological inoculum is rhamnolipid and height
Imitate one of hydrocarbon oxidation bacteria.
7. oil field mining liquid central treating station according to claim 1 or 2 or 3 or 4 or 5 or 6 process for treating oil-containing sludge,
It is characterized in that Hybrid Heating wash temperature is 30 DEG C to 90 DEG C in second step, the additional amount of washing water is thickening sludge weight
2 times；In 4th step, the additional amount of sludge renovation agent is the 1% to 3% of desiccation oily sludge weight.
8. at a kind of implementation oil field mining liquid central treating station as claimed in any of claims 1 to 7 oily sludge
The device of reason method, it is characterised in that wash oil removing including crude oil treating device, sewage-treatment plant, oily sludge heat chemistry
Tank, centrifuge and sludge prosthetic device, fixation is communicated between crude oil treating device water outlet and sewage-treatment plant water inlet
Sewage pipeline, fixation is communicated with the first sludge pipeline between crude oil treating device mud mouth and oily sludge concentration basin mud inlet,
Be communicated with sludge discharge pipeline between sewage-treatment plant mud mouth and the first oily sludge pipeline, oily sludge concentration basin mud mouth with
It is fixed between oily sludge heat chemistry washing oil removing pot mud inlet to be communicated with the second sludge pipeline, on the second oily sludge pipeline according to
It is secondary to be communicated with steam pipe line and washing medicament pipeline, oily sludge heat chemistry wash oil removing pot mud mouth and centrifuge mud inlet it
Between fixation be communicated with third sludge pipeline, it is fixed between centrifuge mud mouth and sludge prosthetic device mud inlet to be communicated with the 4th dirt
Mud pipeline.
9. device according to claim 8, it is characterised in that further include oil slick storage tank, recycle-water surge tank and sludge up to standard
Field is stored, fixation is communicated with oil slick pipeline between oily sludge heat chemistry washing oil removing pot oil outlet and oil slick storage tank oil inlet,
It is fixed between sludge prosthetic device mud mouth and sludge up to standard storage field mud inlet to be communicated with the 5th sludge pipeline, centrifuge water outlet
Fixation is communicated with recycle-water pipeline between mouth and recycle-water surge tank water inlet, and recycle-water surge tank water outlet goes out with steam pipe line
Washing water pipeline is communicated on the second sludge pipeline between mouth and washing agent outlet.
10. device according to claim 8 or claim 9, it is characterised in that third, which contains, is communicated with sludge dehydrating agent pipe on oil pipeline
Line is communicated with sludge renovation agent pipeline on the 4th sludge pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811095451.2A CN108892353A (en) | 2018-09-19 | 2018-09-19 | Oil field mining liquid central treating station process for treating oil-containing sludge and device |
Applications Claiming Priority (1)
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109852416A (en) * | 2018-12-13 | 2019-06-07 | 新疆科力新技术发展股份有限公司 | Oil field central treating station Produced Liquid cryogenic seal interface fast dewatering method and device |
| CN110129016A (en) * | 2019-06-21 | 2019-08-16 | 克拉玛依市建业油田技术服务有限责任公司 | Oily sludge resource utilization tune blocks up preparation |
| CN110590087A (en) * | 2019-07-24 | 2019-12-20 | 中国石油大学(华东) | Treatment method of oily sludge |
| CN112479513A (en) * | 2020-11-06 | 2021-03-12 | 南京工业大学 | Preparation method and application of oil-containing sludge composite curing material |
| CN113003921A (en) * | 2021-03-04 | 2021-06-22 | 山东科技大学 | Method for treating oily sludge by combining hot washing and oxidation |
| CN113003922A (en) * | 2021-03-04 | 2021-06-22 | 山东科技大学 | Integrated efficient hot washing-advanced oxidation combined oily sludge treatment system and oily sludge treatment method |
| CN115746814A (en) * | 2022-11-16 | 2023-03-07 | 河南海纳石油工程技术有限公司 | Efficient environment-friendly blocking remover |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2156275C2 (en) * | 1996-06-11 | 2000-09-20 | Научно-технический центр экологически чистых технологий | Method of processing and reusing petroleum-containing sludges |
| CN101066828A (en) * | 2007-06-12 | 2007-11-07 | 大庆石油学院 | Technological process of treating oil-containing sludge with supercritical water oxidation |
| CN101088942A (en) * | 2006-06-14 | 2007-12-19 | 中国科学院生态环境研究中心 | Process of treating oil-containing sludge |
| CN102001806A (en) * | 2010-12-22 | 2011-04-06 | 朱同德 | Method and device for treating oily sludge |
| CN102849907A (en) * | 2012-09-12 | 2013-01-02 | 余国贤 | Separation method and device of polymer-containing oil sludge |
| CN102863097A (en) * | 2012-09-14 | 2013-01-09 | 濮阳市天地人环保工程技术有限公司 | Standardized treatment reinjection method of sulfur-containing waste liquid of high sulfur-containing oil and gas field |
| CN105198181A (en) * | 2015-05-29 | 2015-12-30 | 新疆科力新技术发展有限公司 | Environment-friendly oil field sludge treating agent and preparation method thereof |
| CN105198180A (en) * | 2015-02-20 | 2015-12-30 | 新疆科力新技术发展有限公司 | Improved water washing treating-agent and method for realizing standard oily sludge treatment in oil field by employing same |
| CN106190891A (en) * | 2016-07-11 | 2016-12-07 | 陕西师范大学 | Based on the oxidation of sodium peroxydisulfate complex and microorganism species biological reinforced Combined Treatment soil with serious petroleum pollution or the method for greasy filth |
| CN106316019A (en) * | 2016-03-22 | 2017-01-11 | 惠州市中环科技环保工程有限公司 | Comprehensive utilization method for petroleum and petrochemical oily sludge resources |
| CN209098478U (en) * | 2018-09-19 | 2019-07-12 | 新疆科力新技术发展股份有限公司 | Oil field mining liquid central treating station oil-bearing sludge treatment equipment |
-
2018
- 2018-09-19 CN CN201811095451.2A patent/CN108892353A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2156275C2 (en) * | 1996-06-11 | 2000-09-20 | Научно-технический центр экологически чистых технологий | Method of processing and reusing petroleum-containing sludges |
| CN101088942A (en) * | 2006-06-14 | 2007-12-19 | 中国科学院生态环境研究中心 | Process of treating oil-containing sludge |
| CN101066828A (en) * | 2007-06-12 | 2007-11-07 | 大庆石油学院 | Technological process of treating oil-containing sludge with supercritical water oxidation |
| CN102001806A (en) * | 2010-12-22 | 2011-04-06 | 朱同德 | Method and device for treating oily sludge |
| CN102849907A (en) * | 2012-09-12 | 2013-01-02 | 余国贤 | Separation method and device of polymer-containing oil sludge |
| CN102863097A (en) * | 2012-09-14 | 2013-01-09 | 濮阳市天地人环保工程技术有限公司 | Standardized treatment reinjection method of sulfur-containing waste liquid of high sulfur-containing oil and gas field |
| CN105198180A (en) * | 2015-02-20 | 2015-12-30 | 新疆科力新技术发展有限公司 | Improved water washing treating-agent and method for realizing standard oily sludge treatment in oil field by employing same |
| CN105198181A (en) * | 2015-05-29 | 2015-12-30 | 新疆科力新技术发展有限公司 | Environment-friendly oil field sludge treating agent and preparation method thereof |
| CN106316019A (en) * | 2016-03-22 | 2017-01-11 | 惠州市中环科技环保工程有限公司 | Comprehensive utilization method for petroleum and petrochemical oily sludge resources |
| CN106190891A (en) * | 2016-07-11 | 2016-12-07 | 陕西师范大学 | Based on the oxidation of sodium peroxydisulfate complex and microorganism species biological reinforced Combined Treatment soil with serious petroleum pollution or the method for greasy filth |
| CN209098478U (en) * | 2018-09-19 | 2019-07-12 | 新疆科力新技术发展股份有限公司 | Oil field mining liquid central treating station oil-bearing sludge treatment equipment |
Non-Patent Citations (1)
| Title |
|---|
| 田中央;尹小明;: "油田污水处理工艺及改进对策", 当代化工研究, no. 07, pages 15 - 16 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109852416A (en) * | 2018-12-13 | 2019-06-07 | 新疆科力新技术发展股份有限公司 | Oil field central treating station Produced Liquid cryogenic seal interface fast dewatering method and device |
| CN110129016A (en) * | 2019-06-21 | 2019-08-16 | 克拉玛依市建业油田技术服务有限责任公司 | Oily sludge resource utilization tune blocks up preparation |
| CN110590087A (en) * | 2019-07-24 | 2019-12-20 | 中国石油大学(华东) | Treatment method of oily sludge |
| CN110590087B (en) * | 2019-07-24 | 2022-07-01 | 中国石油大学(华东) | Treatment method of oily sludge |
| CN112479513A (en) * | 2020-11-06 | 2021-03-12 | 南京工业大学 | Preparation method and application of oil-containing sludge composite curing material |
| CN113003921A (en) * | 2021-03-04 | 2021-06-22 | 山东科技大学 | Method for treating oily sludge by combining hot washing and oxidation |
| CN113003922A (en) * | 2021-03-04 | 2021-06-22 | 山东科技大学 | Integrated efficient hot washing-advanced oxidation combined oily sludge treatment system and oily sludge treatment method |
| CN115746814A (en) * | 2022-11-16 | 2023-03-07 | 河南海纳石油工程技术有限公司 | Efficient environment-friendly blocking remover |
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