CN103936977B - A kind of liquid crude drag reducer and preparation method thereof - Google Patents
A kind of liquid crude drag reducer and preparation method thereof Download PDFInfo
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- CN103936977B CN103936977B CN201410118984.3A CN201410118984A CN103936977B CN 103936977 B CN103936977 B CN 103936977B CN 201410118984 A CN201410118984 A CN 201410118984A CN 103936977 B CN103936977 B CN 103936977B
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- phenol
- amine resin
- drag reducer
- propylene oxide
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Abstract
The invention discloses a kind of liquid crude drag reducer, it is by 1 by phenol-amine resin and propylene oxide：Be polymerized under 10~100 ratio, after formed by organic solvent diluting.The invention also discloses a kind of preparation method of aforesaid liquid drag reducer for crude oil, this method be by phenol-amine resin under conditions of 130 DEG C~140 DEG C with propylene oxide（PO）It is polymerized in claim ratio.Gained drag reducer of the invention forms thin electrolyte film between crude oil macromolecular, on the tube wall of conveyance conduit, reduces flowing crude oil frictional resistance to reach, mentions the purpose of conveying capacity.Meanwhile the product has good dissolving and cleaning performance to the oil base deposit being deposited on feed-line, reduce so as to solve the oil flow channel that pipeline deposition produces, oil pressure rise problem.
Description
Technical field
The present invention relates to a kind of liquid crude drag reducer and preparation method thereof.
Background technology
With the development of world economy, energy demand is growing day by day, and Oil ＆ Gas Storage is the weight for forming energy utilization technology
Want part.In many means of transportation, pipeline transportation have construction speed fast, reduced investment, take up an area less, energy consumption is low, no
Pollute environment, limited the advantages that few by geographical and meteorological condition, and be rapidly developed.At present, what is produced all over the world is exhausted big
Most oil and natural gas pipeline transportations.But pipeline transportation there is also it is serious the shortcomings that, i.e., elastic throughput rate far beyond
Other means of transportation are low.Since during oil exploration, accurate prediction reserves is a very difficult thing, and
Always also there are some uncertain factors for the development prospect in oil field.Even if the reserves in Accurate Determining oil field of having the ability in the future, oil field
Also development period, the phase of abounding with and decline period, and various regions to the demand of oil product also because of expanding economy and the renewal of itself
Regenerate and be varied from, these require that pipeline throughput rate has certain elasticity.In addition, such as pipeline aging causes pressure-resistant performance
Reduce, one of pipeline in parallel occurs that accident needs to overhaul and throughput rate is required for pipeline to have certain tune to throughput rate when also needing to ensure
Energy saving power.The best method to solve the above problems is to use drag reducer.So-called drag reducer, refer to reduce liquid flowing frictional resistance,
Increase the chemical addition agent of throughput rate.It is different using object according to it, the gentle phase drag reduction of water phase drag reducer, oil phase dra can be divided into
Agent.It is known as oil phase dra for the drag reducer in crude oil and its Related product.
Oil phase dra mainly has the function of following several respects：
(1) pipe operations pressure is reduced, improves the safety coefficient of pipeline performance, this is related to national warp in a sense
Ji safety.
(2) if newly-built pipeline considers to use drag reducer in the design process, pipe diameter can be reduced, reduces pump
Scale, so as to greatly save construction investment.
(3) oil product throughput rate can be increased under the conditions of original pipe operations, that is, improves pipe operations efficiency, increase is economical
Benefit.
(4) the more station conveying of oil product can be achieved, close intermediate pump station, save pipe operations cost.
(5) when developing sea, desert, marsh, severe cold areas when the oil field in the severe area of natural conditions, addition can be subtracted
Resist conveying technique is used as conventional, can so increase pumping plant spacing, reduces pumping plant, so that manpower and material resources input are saved,
Increase economic benefit.
(6) quantity for reducing operation pump can be realized in the case where maintaining former throughput rate, not only meets the requirement that pump is safeguarded, but also can
Ensure continuous production.
The drag reducer of traditional poly alpha olefin class is added in oil stream, by distinctive viscoplasticity itself, big point
Subchain is orientated along flow direction natural drawing, this to be orientated the movement for influencing whether fluid particle.The radial effect of fluid particle
Drag reduction agent molecule is set to be distorted, rotational deformation, and drag reduction agent molecule is by the work of intermolecular attractive interaction resistance fluid particle
Firmly, change the action direction and size of fluid particle, make the radial load that flogs a dead horse of a part be converted into following current to axial direction
Power, so as to reduce the consumption of idle work, macroscopically shows the friction loss for reducing fluid, that is, plays the role of drag reduction.
But the drag reducer of this poly alpha olefin class, manufacture craft is considerably complicated, severe reaction conditions, since finished product is
Solid, it is also very cumbersome that scene, which adds technique, and cost is excessively high.
In view of the above circumstances, this problem mainly studies a kind of new liquid crude drag reducer, mainly with deposition theory,
Thin electrolyte film is formed between crude oil macromolecular, on the tube wall of conveyance conduit, flowing crude oil frictional resistance is reduced to reach, mentions conveying capacity
Purpose.Meanwhile the product has good dissolving and cleaning performance to the oil base deposit being deposited on feed-line, so that
Solve the oil flow channel that pipeline deposition produces to reduce, oil pressure rise problem.
The content of the invention
The present invention purpose to be reached：
First purpose of the present invention is to provide for a kind of liquid drag reducer product for Crude Oil Transportation；
Second object of the present invention is to provide a kind of preparation method of the simple drag reducing agent product of operating procedure.
Technical scheme：
A kind of liquid crude drag reducer, it is characterised in that:Its active ingredient is by quality by phenol-amine resin and propylene oxide
Than 1：10~100 macromolecule polyalcohols aggregated into；The phenol-amine resin is the poly- head of phenol-amine resin；The phenol-amine resin gathers head
By hydroquinone and polyethylene polyamine in molar ratio 1:1~5 aggregates into macromolecule polyalcohol；The phenol-amine resin and propylene oxide
Temperature during polymerization is 130~140 DEG C, polymerization pressure≤0.4Mpa.
A kind of preparation method of the liquid crude drag reducer, it is characterised in that：Comprise the following steps：
The first step synthesizes phenol-amine resin
It is 1 in mass ratio by hydroquinone and polyethylene polyamine:1~5 ratio input reaction kettle, is warming up to 40 DEG C~60
DEG C, crosslinking agent is slowly added dropwise, process temperature control is added dropwise, prevents from reacting acutely producing hot-spot, is added dropwise and lifts temperature to 90 DEG C always
Change 1h, be warming up to 100 DEG C~160 DEG C vacuum dehydrations, react and finish after anhydrous steam, cool down, discharge, obtain phenol-amine resin and gather
Head, it is spare；
Second step synthesizes drag reducer
Phenol-amine resin is gathered head to add in polyether reactant kettle, stirring is opened, material is heated to 100 DEG C~l10 DEG C, vacuum
05-0.6h is dehydrated, when being distillated to exclusion, closes vacuum valve, makes in kettle pressure close to -0.08~-0.10 Mpa, by will
The propylene oxide for being slowly passed through metering is sought, controls reaction pressure≤0.4Mpa, reaction temperature is kept for 130~140 DEG C；It is logical to finish, dimension
Reaction temperature is held, continues to stir aging being absorbed into pressure and no longer decline, reaction terminates, and is passed through the aromatic solvent of metering, and mixture is equal
I.e. discharging obtains drag reducer after even, wherein, it is 1 that phenol-amine resin, which gathers head and the aggregate quality ratio of propylene oxide,：10~100.
Phenol-amine resin is synthesized by high-temperature high-pressure reaction kettle, then draws water to obtain poly- head in 100 DEG C~l60 DEG C vacuum.Will be poly-
Head is added in polyether reactant kettle, is opened stirring, material is heated to 100 DEG C~l10 DEG C, vacuum dehydration (about needs 0.5h), to nothing
When moisture content distillates, vacuum valve is closed, makes close -0.08~-0.10 Mpa of pressure in kettle, is slowly passed through the ring of metering on request
Ethylene Oxide, controls reaction pressure≤0.4Mpa, and reaction temperature is kept for 130~140 DEG C；It is logical to finish, reaction temperature is maintained, continues to stir
Aging is absorbed into pressure and no longer declines, and reaction terminates, and is passed through the aromatic solvent of metering, and mixture is uniformly that discharging obtains drag reduction afterwards
Agent.
Beneficial effects of the present invention：
A kind of liquid crude drag reducer of the present invention, forms thin between crude oil macromolecular, on the tube wall of conveyance conduit
Layer liquid film, reduces flowing crude oil frictional resistance to reach, mentions the purpose of conveying capacity.Meanwhile the product is to being deposited on feed-line
Oil base deposit there is good dissolving and cleaning performance so that solve pipeline deposition produce oil flow channel reduce, oil pressure
Rise problem.Also, the drag reducer is compared with other drag reducing agent products, when operating at the scene, it is simple to add technique, security
It is high.
Brief description of the drawings
Fig. 1 is the polymerization process schematic diagram of phenol-amine resin and propylene oxide.
Embodiment
With reference to embodiment, the preparation of liquid crude drag reducer is further elaborated with, but the present invention is not limited to this
A little embodiments.
Embodiment 1
The first step synthesizes phenol-amine resin
It is 1 in mass ratio by hydroquinone and polyethylene polyamine：1 ratio input reaction kettle, is warming up to 40 DEG C~60 DEG C,
Crosslinking agent is slowly added dropwise, process temperature control is added dropwise, prevents from reacting acutely producing hot-spot.It is added dropwise and lifts temperature to 90 DEG C of agings
1h, is warming up to 100 DEG C~160 DEG C vacuum dehydrations, reacts and finish after anhydrous steam, cool down, discharge it is spare.
Second step synthesizes drag reducer
Poly- head is added in polyether reactant kettle, stirring is opened, material is heated to 100 DEG C~l10 DEG C, vacuum dehydration is (about
Need 0.5h), when being distillated to exclusion, vacuum valve is closed, makes close -0.08~-0.10 Mpa of pressure in kettle, by claim
The propylene oxide of metering is slowly passed through, controls reaction pressure≤0.4Mpa, reaction temperature is kept for 130~140 DEG C；It is logical to finish, maintain
Reaction temperature, continues to stir aging being absorbed into pressure and no longer decline, and reaction terminates, and the aromatic solvent of quality such as is passed through, and mixture is equal
I.e. discharging obtains drag reducer after even.
The drag reducing efficiency for detecting this drag reducer is 14.25%.
Embodiment 2
The first step synthesizes phenol-amine resin
By the ratio 1 of hydroquinone and polyethylene polyamine according to claim：2 input reaction kettles, temperature raising to 40 DEG C~60 DEG C,
Crosslinking agent is slowly added dropwise, process temperature control is added dropwise, prevents from reacting acutely producing hot-spot.It is added dropwise and lifts temperature to 90 DEG C of agings
1h, is warming up to 100 DEG C~160 DEG C vacuum dehydrations, reacts and finish after anhydrous steam, cool down, discharge it is spare.
Second step synthesizes drag reducer
Poly- head is added in polyether reactant kettle, stirring is opened, material is heated to 100 DEG C~l10 DEG C, vacuum dehydration is (about
Need 0.5h), when being distillated to exclusion, vacuum valve is closed, makes close -0.08~-0.10 Mpa of pressure in kettle, by claim
The propylene oxide of metering is slowly passed through, controls reaction pressure≤0.4Mpa, reaction temperature is kept for 130~140 DEG C；It is logical to finish, maintain
Reaction temperature, continues to stir aging being absorbed into pressure and no longer decline, reaction terminates, and is passed through the aromatic solvent of metering, and mixture is uniform
It is that discharging obtains drag reducer afterwards, the concentration of drag reducer is 60%.
The drag reducing efficiency for detecting this drag reducer is 14.17%.
Embodiment 3
The first step synthesizes phenol-amine resin,
By the ratio 1 of hydroquinone and polyethylene polyamine according to claim：1.5 input reaction kettles, temperature raising to 40 DEG C~60
DEG C, crosslinking agent is slowly added dropwise, process temperature control is added dropwise, prevents from reacting acutely producing hot-spot.It is added dropwise and lifts temperature to 90 DEG C always
Change 1h, be warming up to 100 DEG C~160 DEG C vacuum dehydrations, react and finish after anhydrous steam, cool down, discharge it is spare.
Second step synthesizes drag reducer
Poly- head is added in polyether reactant kettle, stirring is opened, material is heated to 100 DEG C~l10 DEG C, vacuum dehydration is (about
Need 0.5h), when being distillated to exclusion, vacuum valve is closed, makes close -0.08~-0.10 Mpa of pressure in kettle, by claim
The propylene oxide of metering is slowly passed through, controls reaction pressure≤0.4Mpa, reaction temperature is kept for 130~140 DEG C；It is logical to finish, maintain
Reaction temperature, continues to stir aging being absorbed into pressure and no longer decline, reaction terminates, and the aromatic solvent mixture for being passed through metering is uniform
Afterwards, i.e., discharging obtains drag reducer, and the concentration of drag reducer is 38%.
The drag reducing efficiency for detecting this drag reducer is 14.89%.
Claims (2)
- A kind of 1. liquid crude drag reducer, it is characterised in that:Its active ingredient be by phenol-amine resin and propylene oxide in mass ratio 1：10~100 macromolecule polyalcohols aggregated into；The phenol-amine resin is the poly- head of phenol-amine resin；The phenol-amine resin gather head be by Hydroquinone and polyethylene polyamine in molar ratio 1:1~5 aggregates into macromolecule polyalcohol；The phenol-amine resin and propylene oxide gather Temperature during conjunction is 130~140 DEG C, polymerization pressure≤0.4MPa.
- A kind of 2. preparation method of liquid crude drag reducer according to claim 1, it is characterised in that：Including following step Suddenly：The first step synthesizes phenol-amine resinIt is 1 in mass ratio by hydroquinone and polyethylene polyamine:1~5 ratio input reaction kettle, is warming up to 40 DEG C~60 DEG C, Crosslinking agent is slowly added dropwise, process temperature control is added dropwise, prevents from reacting acutely producing hot-spot, is added dropwise and lifts temperature to 90 DEG C of agings 1h, is warming up to 100 DEG C~160 DEG C vacuum dehydrations, reacts and finish after anhydrous steam, cool down, discharge, obtain phenol-amine resin and gather Head, it is spare；Second step synthesizes drag reducerPhenol-amine resin is gathered head to add in polyether reactant kettle, adds catalyst, stirring is opened, material is heated to 100 DEG C~l10 DEG C, vacuum dehydration 0.5-0.6h, when being distillated to exclusion, closes vacuum valve, makes pressure close -0.08~-0.10 in kettle Mpa, is slowly passed through the propylene oxide of metering on request, controls reaction pressure≤0.4MPa, and reaction temperature is kept for 130~140 DEG C； It is logical to finish, reaction temperature is maintained, continues to stir aging being absorbed into pressure and no longer decline, reaction terminates, and is passed through the aromatic solvent of metering, Mixture is uniformly that discharging obtains drag reducer afterwards, wherein, it is 1 that phenol-amine resin, which gathers head and the aggregate quality ratio of propylene oxide,：10~100 。
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| CN201410118984.3A CN103936977B (en) | 2014-03-27 | 2014-03-27 | A kind of liquid crude drag reducer and preparation method thereof |
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| CN103936977A CN103936977A (en) | 2014-07-23 |
| CN103936977B true CN103936977B (en) | 2018-04-20 |
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| CN114456368B (en) * | 2020-11-10 | 2023-09-22 | 中国石油化工股份有限公司 | Drag reducer for gathering and transporting crude oil and preparation method thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1511920A (en) * | 2002-12-27 | 2004-07-14 | 山东师范大学 | Novel crude oil drag reduction and viscosity reducing agent |
| CN1810933A (en) * | 2006-03-13 | 2006-08-02 | 辽宁奥克化学集团有限公司 | Thick oil demulsifier and its prepn |
| CN103030726A (en) * | 2012-12-27 | 2013-04-10 | 天津市职业大学 | Preparation method of powdered drag reducing agent for crude oil transportation |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7285582B2 (en) * | 2004-12-30 | 2007-10-23 | Conocophillips Company | Modified latex drag reducer and processes therefor and therewith |
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2014
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1511920A (en) * | 2002-12-27 | 2004-07-14 | 山东师范大学 | Novel crude oil drag reduction and viscosity reducing agent |
| CN1810933A (en) * | 2006-03-13 | 2006-08-02 | 辽宁奥克化学集团有限公司 | Thick oil demulsifier and its prepn |
| CN103030726A (en) * | 2012-12-27 | 2013-04-10 | 天津市职业大学 | Preparation method of powdered drag reducing agent for crude oil transportation |
Non-Patent Citations (1)
| Title |
|---|
| 清水型特（超）稠油破乳剂的结构与性能;李岿等;《日用化学品科学》;20060930;第29卷(第9期);第22-28页 * |
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Inventor after: Xiong Guohui Inventor after: Xu Songsong Inventor after: Li Xiaotong Inventor after: Bo Fan Inventor after: Chen Zhengxin Inventor after: Yu Pengxiao Inventor after: Li Peng Inventor after: Yi Hao Inventor before: Cui Lili Inventor before: Zhou Jiancheng Inventor before: Xiong Guohui Inventor before: Ding Dawei Inventor before: Yue Zhentao |
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