CN107805518A - Fail to understand that black suspension thing solid particle removes auxiliary agent and auxiliary agent filling spray nozzle device in crude oil - Google Patents
Fail to understand that black suspension thing solid particle removes auxiliary agent and auxiliary agent filling spray nozzle device in crude oil Download PDFInfo
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- CN107805518A CN107805518A CN201711286949.2A CN201711286949A CN107805518A CN 107805518 A CN107805518 A CN 107805518A CN 201711286949 A CN201711286949 A CN 201711286949A CN 107805518 A CN107805518 A CN 107805518A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
- B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Colloid Chemistry (AREA)
Abstract
The invention discloses fail to understand that black suspension thing solid particle removes auxiliary agent and auxiliary agent filling spray nozzle device in a kind of crude oil.In terms of parts by weight, the auxiliary agent includes following raw material:30~35 parts of propylene glycol block polyether, 1~3 part of glutaraldehyde, 7~10 parts of a alkene sulfonates, 12~18 parts of polyethylene glycol, 12~18 parts of ethylene-vinyl acetate copolymer, 25~30 parts of solvent naphtha.The auxiliary agent can eliminate profit intermediate layer, stable electro-desalting operation, purify draining water quality, lighter oil-soluble black suspension particle is departed from emulsion layer, into crude oil;The inorganic salts of part aqueous reach oil-containing in desalted water and are less than 100ppm, COD is less than 1200ppm through dissolving in after breaking gel in water;Slightly larger insoluble black suspension particle, its aggregation is become bigger particle, deposit to bottom, discharged with water.It can ensure that auxiliary agent uniformly can be sprayed onto in the crude oil of flowing using specific auxiliary agent filling apparatus.
Description
Technical field
The invention belongs to crude oil auxiliary agent technical field, and in particular to fail to understand that black suspension thing solid particle is gone in a kind of crude oil
Except auxiliary agent and auxiliary agent filling spray nozzle device.
Background technology
Due to not clear black suspension particle in the light crude oil in part oil field producing region be present, part petrochina oil plant starts
Because crude quality fluctuation is larger, atmospheric unit long-term operation is influenceed, is mainly manifested in:
(1) electro-desalting and storage are caused between crude oil and water containing the emulsification non-oil thing of shape, the milk density in crude oil
Transport that tank field removing is especially difficult, and especially it is higher to easily cause electric desalting apparatus electric current for the milk, electro-desalting tripping operation frequently occurs,
Have a strong impact on electro-desalting long-term operation.
(2) often there is blackening phenomena in electric desalting apparatus dehydration, and the processing to oil-polluted water causes extreme difficulties, and to complete
Factory's sewage disposal system causes to have a strong impact on the exceeded potential risk of sewage discharge be present.
(3) black suspension thing is carried in crude oil, causes Atmospheric Tower sour water blackening, atmospheric unit normal pressure tower tray floor goes out
Often there is unusual fluctuations, device fortune in existing jelly accumulated plugging tower tray, tower tray fouling, sewage stripping and sulfur recovery facility
There is exceptional hardship in row, seriously restrict the realization of 3 years overhaul targets.
(4) black suspension thing it is affine with sump oil together with, cause oil recovery, freshening system operation abnormal.
As oil field development enters the development of middle and later periods, various chemical oil displacement agents (polymer injection, surfactant, alkali etc.)
And the use of the various chemical agents for increasing production crude oil, the crude oil emulsion that result in output more become to stablizing, profit middle transition
Layer has the trend of progressive additive, black solid particle rich in transition zone, is suspended between crude oil and aqueous phase, and be present in crude oil
In water, a large amount of colloidal state ferrous sulfide particles are contained in this black particle shape material, trickle ferrous sulfide is particle stabilized
Profit transition zone, while the various chemicals in Produced Liquid also enhance the stability of profit transition zone, often cause oil field
The outer oil transportation quality (such as aqueous, saliferous, mechanical admixture) of multi-purpose station electric dehydrator and de- rear sewage quality are exceeded.Outside due to oil field
Contain a large amount of FeS in output oil, there is also Similar Problems in desalting in oil refinery, cause electric desalting apparatus electric field unstable, electricity
Flow higher, the processing especially to oil plant oil-polluted water causes great difficulty.
At present, profit intermediate layer is caused to thicken and the research of processing method for suspended particulate, Chemical for EOR
Focus primarily upon on field joint stations electric dehydrator, it is less to the research of desalting in oil refinery stage, also without a kind of effective
Product and device solve the above problems.
The content of the invention
First technical problem to be solved by this invention, which is to provide in a kind of crude oil, fails to understand black suspension thing solid particle
Auxiliary agent is removed, in terms of parts by weight, the auxiliary agent includes following raw material:30~35 parts of propylene glycol block polyether, 1~3 part of glutaraldehyde,
7~10 parts of a- alkene sulfonates, 12~18 parts of polyethylene glycol, 12~18 parts of ethylene-vinyl acetate copolymer, solvent naphtha 25~30
Part.
Preferably, fail to understand that black suspension thing solid particle removes auxiliary agent, in terms of parts by weight, the auxiliary agent bag in above-mentioned crude oil
Include following raw material:35 parts of propylene glycol block polyether, 1 part of glutaraldehyde, 8 parts of a- alkene sulfonates, 15 parts of polyethylene glycol, ethene-vinegar
Sour 15 parts of ethylene copolymer, 26 parts of solvent naphtha.
Wherein, fail to understand that black suspension thing solid particle is removed in auxiliary agent in above-mentioned crude oil, the propylene glycol block polyether is
L64 or F68.
Wherein, fail to understand that black suspension thing solid particle is removed in auxiliary agent in above-mentioned crude oil, the ethene-vinyl acetate copolymerization
Vinyl acetate content is between 32~40% in thing, and for its molecular weight between 3100~3200, side chain degree is 7.
Wherein, fail to understand that black suspension thing solid particle is removed in auxiliary agent in above-mentioned crude oil, the molecular weight of the polyethylene glycol
Between 500~700.
Wherein, fail to understand that black suspension thing solid particle is removed in auxiliary agent in above-mentioned crude oil, the flash-point of the solvent naphtha is 100
Between~140 DEG C.
Wherein, fail to understand that black suspension thing solid particle is removed in auxiliary agent in above-mentioned crude oil, in addition to 5~8 parts of EDETATE SODIUM salt.
Preferably, fail to understand that black suspension thing solid particle removes auxiliary agent in above-mentioned crude oil, in terms of parts by weight, the auxiliary agent by
Following raw material composition:35 parts of propylene glycol block polyether, 1 part of glutaraldehyde, 8 parts of a- alkene sulfonates, 15 parts of polyethylene glycol, ethene-
15 parts of acetate ethylene copolymer, 26 parts of solvent naphtha, 6 parts of EDETATE SODIUM salt.
Second technical problem to be solved by this invention, which is to provide in above-mentioned crude oil, fails to understand black suspension thing solid particle
Auxiliary agent filling spray nozzle device is removed, the device can ensure that Additives Products are equably sprayed onto in the crude oil of flowing, realize equal
Even mixing.
Fail to understand that black suspension thing solid particle removes auxiliary agent filling spray nozzle device in the crude oil, the device includes filling
Chamber, and ball valve, unidirectional stop valve, annular seal space, high pressure sluice valve and the exploration type nozzle set from top to bottom, the ball valve, list
It is fixedly connected between any two by flange to stop valve, annular seal space and high pressure sluice valve, sets some surround to add in the annular seal space
Note the packing of chamber;The head of the filling chamber connects with ball valve, fills the middle part insertion unidirectional stop valve, annular seal space, high pressure of chamber
Gate valve, filling chamber afterbody are connected with exploration type nozzle;The exploration type nozzle is arranged on crude oil by side line mouth and is responsible for linear diameter
Half at, the opening direction of the exploration type nozzle is 45 °, and is open towards identical with crude oil flow direction of material.
Further, the material of the packing is flexible graphite stuffing.
Further, the filling is arranged on spray nozzle device at the side line mouth of crude oil Trunk Line, and the side line mouth is reserved in
Before crude oil pump or before static mixer.
Further, the ball valve, unidirectional stop valve, high pressure sluice valve, the material of exploration type nozzle are the trade mark
022Cr17Ni12Mo2 stainless steels.
Compared with prior art, the beneficial effects of the invention are as follows:
1st, each composition proportion of auxiliary agent of the present invention is scientific and reasonable, its broken glue, coordination, reduces interfacial tension, wetting infiltration and chela
The physical and chemical principles such as conjunction, can make crude oil collect suspension rapid subsidence or be dissolved in water, eliminate profit intermediate layer, stable electricity
Desalination is run, and purifies draining water quality, lighter oil-soluble black suspension particle is departed from emulsion layer, into crude oil;Part
Water miscible inorganic salts reach oil-containing in desalted water and are less than 100ppm, COD is less than 1200ppm through dissolving in after breaking gel in water;It is slightly larger
Insoluble black suspension particle, its aggregation is become bigger particle, deposit to bottom, discharged with water.
2nd, auxiliary agent filling apparatus provided by the invention can ensure that auxiliary agent uniformly can be sprayed onto in the crude oil of flowing, short
It is sufficiently mixed in time by static mixer with crude oil.
Brief description of the drawings
Fig. 1 is the structural representation of auxiliary agent filling spray nozzle device of the present invention;
Reference:1- fills chamber, 2- ball valves, 3- unidirectional stop valves, 4- annular seal spaces, 5- high pressure sluice valves, the spray of 6- exploration types
Mouth, 7- flanges, 8- packings, 9- crude oil Trunk Lines, 10- side line mouths;
Wherein, ↓ injection direction of auxiliary agent is represented, → crude oil flow direction of material is represented, ┈ represents auxiliary agent and sprayed from exploration type nozzle
Outgoing direction.
Embodiment
, should in terms of parts by weight the invention provides failing to understand that black suspension thing solid particle removes auxiliary agent in a kind of crude oil
Auxiliary agent includes following raw material:30~35 parts of propylene glycol block polyether, 1~3 part of glutaraldehyde, 7~10 parts of a- alkene sulfonates, poly- second
12~18 parts of glycol, 12~18 parts of ethylene-vinyl acetate copolymer, 25~30 parts of solvent naphtha;Wherein, the propylene glycol block gathers
Ether is L64 or F68, and between 32~40%, its molecular weight exists vinyl acetate content in the ethylene-vinyl acetate copolymer
Between 3100~3200, side chain degree is 7;The flash-point of the solvent naphtha is between 100~140 DEG C;The molecule of the polyethylene glycol
Amount is between 500~700.
Preferably, fail to understand that black suspension thing solid particle removes auxiliary agent, in terms of parts by weight, the auxiliary agent bag in above-mentioned crude oil
Include following raw material:35 parts of propylene glycol block polyether, 1 part of glutaraldehyde, 8 parts of a- alkene sulfonates, 15 parts of polyethylene glycol, ethene-vinegar
Sour 15 parts of ethylene copolymer, 26 parts of solvent naphtha.
Wherein, fail to understand that black suspension thing solid particle is removed in auxiliary agent in above-mentioned crude oil, in addition to 5~8 parts of EDETATE SODIUM salt.
Preferably, fail to understand that black suspension thing solid particle removes auxiliary agent in above-mentioned crude oil, in terms of parts by weight, the auxiliary agent by
Following raw material composition:35 parts of propylene glycol block polyether, 1 part of glutaraldehyde, 8 parts of a- alkene sulfonates, 15 parts of polyethylene glycol, ethene-
15 parts of acetate ethylene copolymer, 26 parts of solvent naphtha, 6 parts of EDETATE SODIUM salt.
Fail to understand in crude oil provided by the invention in the component that black suspension thing solid particle removes auxiliary agent, ethyl vinyl acetate second
Alkene polymer and high flash solvent oil have the function that dispersant, stabilization aid Product Status, while auxiliary agent are added in crude oil, can
The viscosity of crude oil is reduced, auxiliary agent is preferably distributed in crude oil.Propylene glycol block polyether can be to profit intermediate layer
Middle black solid particle (containing silt, impurity and a large amount of colloidal state ferrous sulfide particles) carries out brokenly glue, relocation bit, will be trickle
Ferrous sulfide particle aggregation settled down into bulky grain or team shape, other silts and impurity also deposit, and substantially reduce
Content of the black solid particle in crude oil and water.After the completion of broken glue process, in adjuvant component the addition of polyethylene glycol can be used to
Demulsification, the interfacial tension between profit is reduced, accelerate the separating rate of oil and water, and then reduce profit transition region thickness, made
It reaches dynamic equilibrium in a very thin oil-water interfaces.Polyethylene glycol and a- alkene sulfonates in component play wet infiltration
Effect, it is negative for eliminate that the displacement of reservoir oil class chemical agent (such as quaternary ammonium salt, xanthans, polyacrylamide) remained in crude oil brings
Face rings.Glutaraldehyde in component is used for killing the part bacterium in crude oil, and these bacteriums can make to produce H in crude oil2S or other
Disulphide is escaped, and FeS precipitations can be generated with iron reaction.EDETATE SODIUM salt in component is used for chelating inorganic salts in crude oil (such as
NaCl、NaCO3、CaCl2、MgCl2、CaCO3、CaSO4Deng) and part organic metal salt (such as calcium naphthenate, phenol calcium), by salt
Become to be dissolved in the material of water, excluded with sewage.
Further, present invention also offers black suspension thing solid particle removal auxiliary agent filling use is failed to understand in above-mentioned crude oil
Spray nozzle device, the device can ensure that Additives Products are equably sprayed onto in the crude oil of flowing, realize uniformly mixing.The crude oil
In fail to understand that black suspension thing solid particle removes auxiliary agent filling spray nozzle device, the device is including filling chamber 1, and from top to bottom
Ball valve 2, unidirectional stop valve 3, annular seal space 4, high pressure sluice valve 5 and the exploration type nozzle 6 of setting, the ball valve 2, unidirectional stop valve 3,
Annular seal space 4 is fixedly connected by flange 7 between any two with high pressure sluice valve 5, is set in the annular seal space 4 some around filling chamber 1
Packing 8, the material of packing 8 is flexible graphite stuffing;The head of the filling chamber 1 connects with ball valve 2, fills the middle part of chamber 1
Unidirectional stop valve 3, annular seal space 4, high pressure sluice valve 5 are penetrated, the filling afterbody of chamber 1 is connected with exploration type nozzle 6.The filling is filled with nozzle
Put at the side line mouth 10 of crude oil Trunk Line 9, the side line mouth 10 is reserved in before crude oil pump or before static mixer, described
Exploration type nozzle 6 is arranged on by side line mouth 10 at the half of the diameter of crude oil Trunk Line 9, and the exploration type nozzle 6 is opened
Mouth direction is 45 °, and is open towards identical with crude oil flow direction of material.The ball valve 2, unidirectional stop valve 3, high pressure sluice valve 5, probe into
The material of formula nozzle 6 is trade mark 022Cr17Ni12Mo2 stainless steels.
Above-mentioned auxiliary agent filling with spray nozzle device when in use, the crude oil that auxiliary agent is injected in crude oil Trunk Line 9 through filling chamber 1,
By the addition condition of ball valve 2, unidirectional stop valve 3 and high pressure sluice valve 5 to auxiliary agent:Addition, add speed and add pressure, carry out
Regulation, meanwhile, the strict installation site for controlling exploration type nozzle and nozzle opening direction, so as to ensure that Additives Products equably spray
It is spread across in the crude oil of flowing, realizes that auxiliary agent mixes with the uniform of crude oil in the short time, auxiliary agent more conducively of the present invention plays a role.
Above-mentioned auxiliary agent filling spray nozzle device has two selectable filling points, is respectively:
A, before outer output oil enters crude oil storage tank, filling point is before crude oil pump, after injecting, the mixing through crude oil pump, in crude oil
More than 24 hours are stood in storage tank, is taken out of from tank bottom draining by suspended particulate, unreacted complete medicament in part can take to down
The electric desalting apparatus of one step continues to act on.
B, before entering electric desalting apparatus, filling point is before static mixer, after injecting, through static mixer and adjustable mixing
Device fully mixes with crude oil, then through electric field-assisted in electrical desalter, takes suspended particulate out of through electro-desalting draining.
The present invention is made further explanation and description below in conjunction with specific embodiment, but and is not so limited the present invention
Protection domain.
Embodiment 1
Fail to understand that black suspension thing solid particle removes auxiliary agent, including following raw material in crude oil:Propylene glycol block polyether L64
35g, glutaraldehyde 1g, a- alkene sulfonate 8g, Macrogol 600 15g, ethylene-vinyl acetate copolymer (vinyl acetate content
32%, its molecular weight 3100, side chain degree 7) 15g, solvent naphtha (120 DEG C of flash-point) 26g.
Embodiment 2
Fail to understand that black suspension thing solid particle removes auxiliary agent, including following raw material in crude oil:Propylene glycol block polyether F68
35g, glutaraldehyde 1g, a- alkene sulfonate 8g, Macrogol 600 15g, ethylene-vinyl acetate copolymer (vinyl acetate content
35%, its molecular weight 3200, side chain degree 7) 15g, solvent naphtha (120 DEG C of flash-point) 26g, EDETATE SODIUM salt 6g.
Embodiment 3
Fail to understand that black suspension thing solid particle removes auxiliary agent, including following raw material in crude oil:Propylene glycol block polyether F68
30g, glutaraldehyde 3g, a- alkene sulfonate 10g, the 12g of polyethylene glycol 500, ethylene-vinyl acetate copolymer (vinyl acetate content
40%, its molecular weight 3200, side chain degree 7) 12g, solvent naphtha (130 DEG C of flash-point) 30g.
Embodiment 4
Fail to understand that black suspension thing solid particle removes auxiliary agent, including following raw material in crude oil:Propylene glycol block polyether F68
33g, glutaraldehyde 2g, a- alkene sulfonate 7g, the 18g of polyethylene glycol 700, ethylene-vinyl acetate copolymer (vinyl acetate content
38%, its molecular weight 3160, side chain degree 7) 18g, solvent naphtha (140 DEG C of flash-point) 25g, EDETATE SODIUM salt 8g.
The adding amount of above-mentioned auxiliary agent is 20~50ppm/ single-stages using crude runs as radix.Each composition of auxiliary agent of the present invention
Match scientific and reasonable, its broken glue, coordination, reduce the physical and chemical principles such as interfacial tension, wetting infiltration and chelating, crude oil can be made to converge
Total suspended matter rapid subsidence is dissolved in water, eliminates profit intermediate layer, stable electro-desalting operation, purifies draining water quality, make compared with
Light oil-soluble black suspension particle departs from emulsion layer, into crude oil;The inorganic salts of part aqueous through dissolving in after breaking gel
In water, reach oil-containing in desalted water and be less than 100ppm, COD is less than 1200ppm;Slightly larger insoluble black suspension particle, makes it
Aggregation becomes bigger particle, deposits to bottom, is discharged with water.
Claims (10)
1. fail to understand that black suspension thing solid particle removes auxiliary agent in crude oil, it is characterised in that in terms of parts by weight, the auxiliary agent includes
Following raw material:30~35 parts of propylene glycol block polyether, 1~3 part of glutaraldehyde, 7~10 parts of a- alkene sulfonates, polyethylene glycol 12~
18 parts, 12~18 parts of ethylene-vinyl acetate copolymer, 25~30 parts of solvent naphtha.
2. according to failing to understand that black suspension thing solid particle removes auxiliary agent in the crude oil described in claim 1, it is characterised in that with
Parts by weight meter, the auxiliary agent include following raw material:35 parts of propylene glycol block polyether, 1 part of glutaraldehyde, 8 parts of a- alkene sulfonates, gather
15 parts of ethylene glycol, 15 parts of ethylene-vinyl acetate copolymer, 26 parts of solvent naphtha.
3. fail to understand that black suspension thing solid particle removes auxiliary agent in crude oil according to claim 1 or 2, it is characterised in that
The propylene glycol block polyether is L64 or F68;Vinyl acetate content is 32~40% in the ethylene-vinyl acetate copolymer
Between, for its molecular weight between 3100~3200, side chain degree is 7.
4. fail to understand that black suspension thing solid particle removes auxiliary agent in crude oil according to claim 1 or 2, it is characterised in that
The flash-point of the solvent naphtha is between 100~140 DEG C, and the molecular weight of the polyethylene glycol is between 500~700.
5. fail to understand that black suspension thing solid particle removes auxiliary agent, its feature in the crude oil according to any one of Claims 1 to 4
It is, the auxiliary agent also includes 5~8 parts of EDETATE SODIUM salt.
6. fail to understand that black suspension thing solid particle removes auxiliary agent in crude oil according to claim 5, it is characterised in that with weight
Number meter is measured, the auxiliary agent is made up of following raw material:35 parts of propylene glycol block polyether, 1 part of glutaraldehyde, 8 parts of a- alkene sulfonates, gather
15 parts of ethylene glycol, 15 parts of ethylene-vinyl acetate copolymer, 26 parts of solvent naphtha, 6 parts of EDETATE SODIUM salt.
7. fail to understand that black suspension thing solid particle removes auxiliary agent filling and filled with nozzle in any one of claim 1~6 crude oil
Put, it is characterised in that the device include filling chamber, and set from top to bottom ball valve, unidirectional stop valve, annular seal space, high pressure
Gate valve and exploration type nozzle, the ball valve, unidirectional stop valve, annular seal space and high pressure sluice valve are fixed by flange between any two to be connected
Connect, some packings around filling chamber are set in the annular seal space;The head of the filling chamber connects with ball valve, fills in chamber
Portion's insertion unidirectional stop valve, annular seal space, high pressure sluice valve, filling chamber afterbody are connected with exploration type nozzle;The exploration type nozzle leads to
Side line mouth is crossed at the half of crude oil supervisor's linear diameter, the opening direction of the exploration type nozzle is 45 °, and is open
Direction is identical with crude oil flow direction of material.
8. fail to understand that black suspension thing solid particle removes auxiliary agent filling spray nozzle device in crude oil according to claim 7, its
It is characterised by, the material of the packing is flexible graphite stuffing.
9. fail to understand that black suspension thing solid particle removes auxiliary agent filling spray nozzle device in crude oil according to claim 7, its
It is characterised by, the filling is arranged on spray nozzle device at the side line mouth of crude oil Trunk Line, before the side line mouth is reserved in crude oil pump
Or before static mixer.
10. fail to understand that black suspension thing solid particle removes auxiliary agent filling spray nozzle device in crude oil according to claim 7, its
It is characterised by, the ball valve, unidirectional stop valve, high pressure sluice valve, the material of exploration type nozzle are trade mark 022Cr17Ni12Mo2
Stainless steel.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109589813A (en) * | 2018-12-07 | 2019-04-09 | 国电科学技术研究院有限公司 | Mix dispenser in more rotation jet stream whirlpools |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63256685A (en) * | 1987-04-15 | 1988-10-24 | Kashima Sekiyu Kk | Injection fluid composition for recovery of petroleum |
RU2211097C1 (en) * | 2002-02-01 | 2003-08-27 | Ходырев Александр Иванович | Injector unit for injection of liquid into gas line |
CN101050382A (en) * | 2007-05-14 | 2007-10-10 | 北京科技大学 | Deemulsifier for lowering FcS content in drainage of electrical desalting /dewatering, and preparation method |
CN101875839A (en) * | 2009-04-30 | 2010-11-03 | 中国石油天然气股份有限公司 | Multifunctional preparation for controlling biological corrosion and blockage of oilfield production system |
CN102127409A (en) * | 2011-01-10 | 2011-07-20 | 中国科学院化学研究所 | Crude oil viscosity-breaking pour-point depressant composition, and preparation method and application thereof |
CN104018966A (en) * | 2014-05-29 | 2014-09-03 | 哈尔滨工程大学 | Pressure accumulation flow-limiting type electromagnetic control oil sprayer |
CN106281289A (en) * | 2016-08-18 | 2017-01-04 | 克拉玛依新科澳石油天然气技术股份有限公司 | Recover the oil with pour-viscosity reduction dehydrant and preparation method thereof |
-
2017
- 2017-12-07 CN CN201711286949.2A patent/CN107805518A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63256685A (en) * | 1987-04-15 | 1988-10-24 | Kashima Sekiyu Kk | Injection fluid composition for recovery of petroleum |
RU2211097C1 (en) * | 2002-02-01 | 2003-08-27 | Ходырев Александр Иванович | Injector unit for injection of liquid into gas line |
CN101050382A (en) * | 2007-05-14 | 2007-10-10 | 北京科技大学 | Deemulsifier for lowering FcS content in drainage of electrical desalting /dewatering, and preparation method |
CN101875839A (en) * | 2009-04-30 | 2010-11-03 | 中国石油天然气股份有限公司 | Multifunctional preparation for controlling biological corrosion and blockage of oilfield production system |
CN102127409A (en) * | 2011-01-10 | 2011-07-20 | 中国科学院化学研究所 | Crude oil viscosity-breaking pour-point depressant composition, and preparation method and application thereof |
CN104018966A (en) * | 2014-05-29 | 2014-09-03 | 哈尔滨工程大学 | Pressure accumulation flow-limiting type electromagnetic control oil sprayer |
CN106281289A (en) * | 2016-08-18 | 2017-01-04 | 克拉玛依新科澳石油天然气技术股份有限公司 | Recover the oil with pour-viscosity reduction dehydrant and preparation method thereof |
Non-Patent Citations (1)
Title |
---|
吴迪等: "用表面活性剂和硫化物去除剂协同处理含硫化亚铁颗粒污油", 《精细与专用化学品》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109589813A (en) * | 2018-12-07 | 2019-04-09 | 国电科学技术研究院有限公司 | Mix dispenser in more rotation jet stream whirlpools |
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