CN207468426U - A kind of F-T synthetic waters phase processor device - Google Patents
A kind of F-T synthetic waters phase processor device Download PDFInfo
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- CN207468426U CN207468426U CN201721386513.6U CN201721386513U CN207468426U CN 207468426 U CN207468426 U CN 207468426U CN 201721386513 U CN201721386513 U CN 201721386513U CN 207468426 U CN207468426 U CN 207468426U
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Abstract
The utility model discloses a kind of F T synthetic waters phase processor devices, are related to the processing unit of synthetic water；Including heavy paraffin hydrocarbon settling tank, the high-precision oil water separators of F T, heavy paraffin hydrocarbon settling tank is connected with the high-precision oil water separators of F T, the top of the high-precision oil water separators of F T is connected by third pipeline with light paraffins tank, bottom is connected by second pipe with synthesis water pot, densimeter is respectively provided on second pipe and third pipeline, synthesis water pot is connected by the 4th pipeline with biochemical treatment equipment, and the 4th pipeline is provided with synthetic water booster pump；Heavy paraffin hydrocarbon is settled pot bottom synthetic water pipeline technological transformation to F- T synthesis water pot is removed by the utility model, and the synthetic water come from tank field is directly entered synthesis water pot, and the run time of oil water separator is reduced after technological transformation, reduces maintenance cost.
Description
Technical field
The utility model is related to the processing unit of synthetic water, to get along specifically, the utility model is related to a kind of F-T synthetic waters
Manage device.
Background technology
Development of coal liquefaction has become the long-range Strategic Measure that China solves contradiction between oil supply and demand, and Fischer-Tropsch synthesis is
The core reaction of indirect coal liquefaction, usually said F- T synthesis refer to, the synthesis gas made of coal or natural gas（H2+CO）
By iron-based, cobalt-based, iron cobalt-base catalyst, the reaction of HC fuel and industrial chemicals is converted under certain temperature and pressure,
The hydrocarbon of different chain length can obtain the oil products such as gasoline, diesel oil, kerosene and multi-chemical after processing modifies, and can by-product it is hard
Wax, tail gas can obtain low-carbon alkene through cryogenic separation or increases oil product yield through oligomerisation reaction or returned through being restructured as synthesis gas
For synthesizing hydrocarbon, release gas can be used for heat supply, power generation or synthesis ammonia etc..F- T synthesis has relative to direct liquefaction to raw material
Strong applicability, the characteristics of product category is more, institute's oil-producing quality is high.
While Synthin fuel, the heavy paraffin hydrocarbon of generation is settled F- T synthesis, and synthetic water can not be straight
Tap into capable processing, the long operational time of oil water separator, maintenance cost height.
Utility model content
More than the utility model overcomes the problems, such as, it is contemplated that process pipelines structure situation, after process pipelines are transformed again
Layout, the simple operability of route after change are stronger.The run time of oil water separator is reduced, reduces maintenance cost.
The utility model overcome the deficiencies in the prior art, the technical problem to be solved is that provide a kind of F-T synthesis water phase
The separator of middle light paraffins.In order to solve the above technical problems, technical solution is used by the utility model：Including heavy
The high-precision oil water separator of alkane settling tank, F-T, it is characterised in that the heavy paraffin hydrocarbon settling tank passes through first pipe and F-T
High-precision oil water separator is connected, and the top of the high-precision oil water separators of the F-T passes through third pipeline and light paraffins tank phase
It connects, is provided with the first densimeter on the third pipeline, is connected between first densimeter and light paraffins tank
There is one end of the 5th pipeline, the other end of the 5th pipeline is connected with heavy paraffin hydrocarbon settling tank；The F-T high essential oils
The bottom of separator is connected by second pipe with synthesis water pot, and the second densimeter is provided on the second pipe,
Be connected with one end of the 6th pipeline between second densimeter and synthesis water pot, the other end of the 6th pipeline with
Heavy paraffin hydrocarbon settling tank is connected；The synthesis water pot is connected by the 4th pipeline with biochemical treatment equipment, and the described the 4th
Pipeline is provided with synthetic water booster pump.
The utility model has the advantages that compared with prior art：
Heavy paraffin hydrocarbon is settled pot bottom synthetic water pipeline technological transformation to F- T synthesis water pot is removed by the utility model, from tank field mistake
The synthetic water come is directly entered synthesis water pot, is sent again to biochemistry by synthetic water booster pump, and high-precision oil water separator
The oil water mixture for receiving separator carries out water-oil separating, and light paraffins remove tank field light paraffins tank through high fine seperator top,
Synthetic water removes synthesis water pot through high-precision separator bottom, is sent to biochemistry and is handled again by synthetic water booster pump, dropped after technological transformation
The low run time of oil water separator reduces maintenance cost.
Description of the drawings
The utility model is described in more detail below in conjunction with the accompanying drawings.
Fig. 1 is the structure diagram of the utility model.
In figure, 1 is heavy paraffin hydrocarbon settling tank, and 2 be the high-precision oil water separators of F-T, and 3 be light paraffins tank, and 4 be synthetic water
Tank, 5 be synthetic water booster pump, and 6 be biochemical treatment equipment, and 7 be first pipe, and 8 be second pipe, and 9 be third pipeline, and 10 be the 4th
Pipeline, 11 be the second densimeter, and 12 be the first densimeter, and 13 be the 6th pipeline, and 14 be the 5th pipeline.
Specific embodiment
As shown in Figure 1, a kind of F-T synthetic waters phase processor device of the utility model, including heavy paraffin hydrocarbon settling tank 1, F-T high
Essential oil separator 2, the heavy paraffin hydrocarbon settling tank 1 are connected by the oil water separator 2 high-precision with F-T of first pipe 7, institute
The top of the high-precision oil water separators 2 of F-T stated is connected by third pipeline 9 with light paraffins tank 3, the third pipeline 9
On be provided with the first densimeter 12, be connected with the 5th pipeline 14 between first densimeter 12 and light paraffins tank 3
One end, the other end of the 5th pipeline 14 are connected with heavy paraffin hydrocarbon settling tank 1；The high-precision oil water separators 2 of the F-T
Bottom by second pipe 8 with synthesis water pot 4 be connected, the second densimeter 11 is provided on the second pipe 8, in institute
Be connected with one end of the 6th pipeline 13 between the second densimeter 11 for stating and synthesis water pot 4, the 6th pipeline 13 it is another
End is connected with heavy paraffin hydrocarbon settling tank 1；The synthesis water pot 4 is connected by the 4th pipeline 10 with biochemical treatment equipment 6, institute
The 4th pipeline 10 stated is provided with synthetic water booster pump 5.
The use process of the utility model：
In process of production, 1 bottom synthetic water of tank field heavy paraffin hydrocarbon settling tank enters through LO-1704-65-E2F51 pipelines
The high-precision oil water separator 2 of Fischer-Tropsch carries out water-oil separating, and light paraffins pass through the through high-precision 2 top third pipeline 9 of oil water separator
During one densimeter 12, as proportion ＜ 0.9g/cm3, light paraffins tank 3 is removed, as proportion >=0.9g/cm3, the lightweight alkane by separation
The 5th pipeline 14 of hydrocarbon clearance flow back into heavy paraffin hydrocarbon settling tank 1.
Second pipe 8 of the synthetic water through high 2 bottom of fine seperator by separation, during by the second densimeter 11, when than
Focus on 0.9-0.98g/cm3, synthesis water pot 4 is removed, is sent again to biochemical treatment equipment 6 by synthetic water booster pump 5；As proportion ＜
0.9g/cm3, the synthetic water by separation flow back into heavy paraffin hydrocarbon settling tank 1 by the 6th pipeline 13, re-starts grease point
From；Since oil content is less than the processing index of oil water separator from the synthetic water that heavy paraffin hydrocarbon settling tank comes in actual production
200ppm, and less than biochemical influent quality standard 500ppm, biochemical treatment can be immediately discharged to.
The embodiments of the utility model have been described in detail above with reference to the accompanying drawings, but the utility model is not limited to
Embodiment is stated, within the knowledge of a person skilled in the art, the utility model aims can also not departed from
Under the premise of various changes can be made.
Claims (1)
1. a kind of F-T synthetic waters phase processor device, including heavy paraffin hydrocarbon settling tank（1）, the high-precision oil water separators of F-T（2）, it is special
Sign is the heavy paraffin hydrocarbon settling tank（1）Pass through first pipe（7）With the high-precision oil water separators of F-T（2）It is connected, it is described
The high-precision oil water separators of F-T（2）Top pass through third pipeline（9）With light paraffins tank（3）It is connected, the third pipe
Road（9）On be provided with the first densimeter（12）, in first densimeter（12）With light paraffins tank（3）Between be connected with
Five pipelines（14）One end, the 5th pipeline（14）The other end and heavy paraffin hydrocarbon settling tank（1）It is connected；The F-
The high-precision oil water separators of T（2）Bottom pass through second pipe（8）With synthesizing water pot（4）It is connected, the second pipe（8）
On be provided with the second densimeter（11）, in second densimeter（11）With synthesis water pot（4）Between be connected with the 6th pipeline
（13）One end, the 6th pipeline（13）The other end and heavy paraffin hydrocarbon settling tank（1）It is connected；The synthesis water pot
（4）Pass through the 4th pipeline（10）With biochemical treatment equipment（6）It is connected, the 4th pipeline（10）It is provided with synthetic water booster pump
（5）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721386513.6U CN207468426U (en) | 2017-10-25 | 2017-10-25 | A kind of F-T synthetic waters phase processor device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721386513.6U CN207468426U (en) | 2017-10-25 | 2017-10-25 | A kind of F-T synthetic waters phase processor device |
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| CN207468426U true CN207468426U (en) | 2018-06-08 |
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| CN201721386513.6U Active CN207468426U (en) | 2017-10-25 | 2017-10-25 | A kind of F-T synthetic waters phase processor device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107721071A (en) * | 2017-10-25 | 2018-02-23 | 山西潞安煤基精细化学品有限公司 | F T synthetic water phase processor devices |
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2017
- 2017-10-25 CN CN201721386513.6U patent/CN207468426U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107721071A (en) * | 2017-10-25 | 2018-02-23 | 山西潞安煤基精细化学品有限公司 | F T synthetic water phase processor devices |
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| TR01 | Transfer of patent right |
Effective date of registration: 20190124 Address after: 046204 No. 1 Luan Street, Houbao Town, Xiangyuan County, Changzhi City, Shanxi Province Co-patentee after: Shanxi Lu'an coal based Fine Chemicals Co. Ltd. Patentee after: Shanxi Lu'an Mining Industry (Group) Co., Ltd. Address before: 047500 Caogou Village, Dianshang Town, Lucheng City, Changzhi City, Shanxi Province Patentee before: Shanxi Lu'an coal based Fine Chemicals Co. Ltd. |