CN205011707U - Diesel oil dewatering device - Google Patents
Diesel oil dewatering device Download PDFInfo
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- CN205011707U CN205011707U CN201520403674.6U CN201520403674U CN205011707U CN 205011707 U CN205011707 U CN 205011707U CN 201520403674 U CN201520403674 U CN 201520403674U CN 205011707 U CN205011707 U CN 205011707U
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- diesel oil
- coalescence
- dewatering device
- separator
- oil
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Abstract
The utility model relates to a diesel oil dewatering device, it includes: prefilter and coalescence -separation ware, prefilter's oil -out links to each other with the oil inlet of coalescence -separation ware, the coalescence -separation ware include: center distributing pipe, coalescent pack layer, coalescence filter cartridge layer, filtering separator and salt deposit, wherein the oil inlet of central distributing pipe and coalescence -separation ware link to each other, the coalescent pack layer periphery of establishing the centering distributing pipe, coalescence filter cartridge layer set up in the periphery on coalescent pack layer, the oil -out of filtering separator and coalescence -separation ware link to each other, filtering separator's inside is equipped with the salt deposit. The utility model discloses gather knot, coalescence filtration, filtering separation and salt drying in an organic whole, the small investment, the flow is short, separation efficiency is high, strong adaptability, anti surface -activeagent contamination can be good, area is little and easy operation maintenance.
Description
Technical field
The utility model relates to Petroleum Processing Technology field, especially about a kind of adopt the drying of coalescent, coalescence filtration, filtering separation and salt remove a small amount of moisture content in diesel oil, the diesel oil dewatering device of the oil dehydrating process be suitable in various technique.
Background technology
The main path in diesel oil source is obtained by crude oil processing, according to the difference of processing mode, is divided into: normal pressure straight-run diesel oil, catalytic cracking diesel oil and hydrogenated diesel oil.Diesel oil is one of main products of refining of petroleum, because can use water vapour containing in moisture content and the course of processing in stock oil, also can carry a small amount of moisture content when therefore going out device in diesel oil.But the main application of diesel oil is as oil fuel, in fuel diesel, the content requirement of moisture content is very strict, and the water content I class diesel oil of world fuel standards diesel oil is not more than 500mg/kg, and other is not more than 200mg/kg, therefore needs to carry out processed to diesel oil.Diesel oil dewatering belongs to liquid-liquid heterogeneous separation technique, and liquid-adoptable equipment of liquid heterogeneous separation has settlement separator, cyclone separator, coalescing separator, membrane separation apparatus etc., and the occasion of the object that a few kind equipment is suitable for and use is often different.Although the separation efficiency of membrane sepn is very high, cost is also very high, because flux is little, equipment is also very huge.
Chinese patent application CN1654108 discloses a kind of low temperature phase change liquid-liquid separation thickener, utilizes the difference of two kinds of freezing points, adopts unit cooler that water-setting is build-up ice, and last ice sheet is got skates by planing pattern and dug to reach the concentrated object of mixed liquid.This invention is applicable to the situation of little treatment capacity, and energy consumption is high, complex process.
Chinese patent CN101037608 provides a kind of diesel oil hydrogenation refining fractionation method, comprises a reaction and generates oil vapour stripping fractionation process and a refined diesel oil dehydration.Its concrete technical scheme is: the hydrofining reaction come by light pressure separator generates oil enters separation column opening for feed with certain temperature, separation column adopts steam stripped fractionation, overheated stripped vapor is passed at the bottom of tower, tower top oil gas enters return tank of top of the tower after cooling, refined diesel oil at the bottom of tower enters the vertical electric of one or more series connection from water knockout by topping-up pump supercharging after heat exchange cools, by the high-voltage electric field effect in ionization water knockout, the preventing trace amount of steam condensed water in refined diesel oil is gathered at the bottom of larger drops of water fall down to tank also to be taken off by dehydration pipeline, water-free refined diesel oil out becomes the qualified refined diesel oil product of indices afterwards from the top of ionization water knockout.But high tension electrostatic field is introduced need consume electric energy.
Chinese patent CN102234525A discloses a kind of method reducing water content in hydrocarbon oil, and wherein, the method comprises and being contacted with the aqueous solution of salt by hydrocarbon ils, and the product after contact is carried out oily water separation.This invention contacts with the aqueous solution of salt by making hydrocarbon ils, and the product after contact is carried out oily water separation, successfully achieves the target reduced by the water-content of hydrocarbon ils.Be applicable to the dehydration of the hydrocarbon ils from hydrofining, hydrocracking, catalytic cracking and atmospheric and vacuum distillation unit, not only can remove free-water completely, and effectively can remove at least part of dissolved water in hydrocarbon ils.But need a large amount of salt solution, device is huge.
Adopt coalescer dehydration to be common another kind of dewatering both at home and abroad, the method has significantly de-free-water effect for lightweight oil.But or diesel oil containing more mechanical impurity large for water-content superelevation or density, viscosity or lubricating oil, DeGrain or substantially do not have effect.
As can be seen here, above-mentioned existing diesel oil dewatering device with in use in structure, obviously still has inconvenience and defect, and is urgently further improved.In order to solve above-mentioned Problems existing, relevant manufactures there's no one who doesn't or isn't seeks solution painstakingly, but have no applicable design for a long time to be completed by development, and common product does not have appropriate structure to solve the problem, this is obviously the anxious problem for solving of relevant dealer always.
Summary of the invention
The purpose of this utility model is to provide a kind of diesel oil dewatering device, technical problem to be solved is, gather knot, coalescence filtration, filtering separation and salt dry in one, less investment, flow process are short, separation efficiency is high, strong adaptability, resistance to surface active agent pollution performance are good, floor space is little and maintenance easy to operate.
The purpose of this utility model realizes by the following technical solutions.The utility model proposes a kind of diesel oil dewatering device, it comprises: prefilter and coalescing separator, and the oil outlet of prefilter is connected with the oil-in of coalescing separator; Described coalescing separator comprises: central dispense pipe, coalescent pack layer, Coalescence filter core layer, filter separator and salt deposit, wherein said central dispense pipe is connected with the oil-in of coalescing separator, described coalescent pack layer is arranged at the periphery of central dispense pipe, described Coalescence filter core layer is arranged at the periphery of coalescent pack layer, described filter separator is connected with the oil outlet of coalescing separator, and the inside of filter separator is provided with described salt deposit.
The purpose of this utility model also can be applied to the following technical measures to achieve further.
Preferably, aforesaid diesel oil dewatering device, wherein said salt deposit is Industrial Salt.
Preferably, aforesaid diesel oil dewatering device, wherein said Industrial Salt is sodium-chlor.
Preferably, aforesaid diesel oil dewatering device, the filtering accuracy of wherein said prefilter is 50-200 micron.
Preferably, aforesaid diesel oil dewatering device, wherein said coalescent pack layer is coalescent metal, pottery or glass.
Preferably, aforesaid diesel oil dewatering device, wherein said Coalescence filter core layer is glass fibre, metal, trevira or pottery.
Preferably, aforesaid diesel oil dewatering device, wherein said filter separator skin is organic coating, and this organic coating is tetrafluoroethylene or vinylidene.
Preferably, aforesaid diesel oil dewatering device, wherein said prefilter is one or more.
Preferably, aforesaid diesel oil dewatering device, wherein said coalescing separator is one or more.
By technique scheme, diesel oil dewatering device of the present utility model at least has following advantages and beneficial effect: diesel oil dewatering device of the present utility model adopts coalescent, coalescence filtration, a small amount of moisture content in diesel oil is removed in filtering separation and salt drying, the qualified diesel oil of below 200mg/kg is down to the water-content obtained in diesel oil, be suitable for the oil dehydrating process in various technique, also the processed of various hydrocarbon ils is suitable for, there is less investment, flow process is short, separation efficiency is high, strong adaptability, resistance to surface active agent pollution performance is good, floor space is little, and the advantages such as maintenance easy to operate.
Above-mentioned explanation is only the general introduction of technical solutions of the utility model, in order to technique means of the present utility model can be better understood, and can be implemented according to the content of specification sheets, and can become apparent to allow above and other object of the present utility model, feature and advantage, below especially exemplified by preferred embodiment, and coordinate accompanying drawing, be described in detail as follows.
Accompanying drawing explanation
Fig. 1 is the connection diagram of diesel oil dewatering device of the present utility model.
Fig. 2 is the structural representation of coalescing separator of the present utility model.
[main element nomenclature]
1: diesel oil import 2: coalescent pack layer
3: Coalescence filter core layer 4: shell
5: end socket 6: filter separator
7: salt deposit 8: diesel oil exports
9: interfacial meter mouth 10: water port
11: central dispense pipe 12: prefilter
13: coalescing separator 14: diesel oil
15: dehydration diesel oil 16: sewage
Embodiment
For further setting forth the utility model for the technique means reaching predetermined goal of the invention and take and effect, below in conjunction with accompanying drawing and preferred embodiment, to according to the embodiment of a kind of diesel oil dewatering device that the utility model proposes, structure, feature and effect thereof, be described in detail as follows.
Referring to Fig. 1, is the connection diagram of diesel oil dewatering device of the present utility model.Comprise: prefilter 12 and coalescing separator 13, wherein, the oil outlet of prefilter 12 connects the oil-in of coalescing separator 13.
Prefilter 12 is filtering accuracies is the various strainers of 50-200 μm, with the various solid particulate matters in filtered fuel.
Refer to Fig. 2, it is the structural representation of coalescing separator 13, current collection is coalescent, coalescence filtration, filtering separation and salt drying are in one, the inside of its shell 4 is provided with: coalescent pack layer 2, Coalescence filter core layer 3, central dispense pipe 11, filter separator 6, wherein, central dispense pipe 11 is connected with the diesel oil import 1 of coalescing separator 13, coalescent pack layer 2 is arranged at the periphery of central dispense pipe 11, preferably, coalescent pack layer 2 is coalescent metal, the coalescence materials such as pottery or glass, therefore moisture diesel oil first enters coalescent pack layer 2 through central dispense pipe 11, at coalescent pack layer 2 first through coalescent, part emulsion breakdown of emulsion is made to make the globule coalescent, block a part of tensio-active agent simultaneously, protect Coalescence filter core, thus extended period life cycle.Coalescence filter core layer 3 is arranged at the periphery of coalescent pack layer 2, and Coalescence filter core layer 3 can be the water wetted materials such as glass fibre, metal, trevira or pottery.Filter separator 6 exports 8 with the diesel oil of coalescing separator 13 and is connected, and filter separator 6 skin is organic coating, as the hydrophobic material such as tetrafluoroethylene, vinylidene, make oil by and water only.The inside of filter separator 6 is provided with salt deposit 7, and preferably, salt deposit 7 is Industrial Salt, such as sodium-chlor.A small amount of water, contact with Industrial Salt, further coalescent breakdown of emulsion by after filter separator 6 with the form of microemulsion and dissolved water, sloughs micro-water.The top of shell 4 is provided with end socket 5, below is provided with water port 10, side is provided with interfacial meter mouth 9.Preferably, the pressure-losses of coalescing separator 13 is 0.05-0.15MPa, and the service temperature of diesel oil is 20-80 DEG C, and the water-content in diesel oil is 200-10000mg/kg.
Working process of the present utility model is as follows: diesel oil 14 is first through prefilter 12, filter the particulate matter such as coke powder, then coalescing separator 13 is entered, dry through voltolisation knot, coalescence filtration, filtering separation and salt, dehydration diesel oil 15 after dehydration goes out device, and the sewage 16 deviate from enters Sewage treatment systems.
In the utility model, at least comprise one or more prefilter 12 and one or more coalescing separator 13, can skid-mounted device be made.
Concrete, illustrate implementation result of the present utility model: the hydrogenated diesel oil of moisture 450mg/kg, under 35 DEG C of temperature, 0.4MPa pressure, filter pressure drop 0.1MPa, after this technical finesse, diesel oil is moisture is down to 160mg/kg.
The above, it is only preferred embodiment of the present utility model, not any pro forma restriction is done to the utility model, although the utility model discloses as above with preferred embodiment, but and be not used to limit the utility model, any those skilled in the art, do not departing within the scope of technical solutions of the utility model, make a little change when the technology contents of above-mentioned announcement can be utilized or be modified to the Equivalent embodiments of equivalent variations, in every case be the content not departing from technical solutions of the utility model, according to any simple modification that technical spirit of the present utility model is done above embodiment, equivalent variations and modification, all still belong in the scope of technical solutions of the utility model.
Claims (9)
1. a diesel oil dewatering device, is characterized in that comprising: prefilter and coalescing separator, and the oil outlet of prefilter is connected with the oil-in of coalescing separator; Described coalescing separator comprises: central dispense pipe, coalescent pack layer, Coalescence filter core layer, filter separator and salt deposit, wherein said central dispense pipe is connected with the oil-in of coalescing separator, described coalescent pack layer is arranged at the periphery of central dispense pipe, described Coalescence filter core layer is arranged at the periphery of coalescent pack layer, described filter separator is connected with the oil outlet of coalescing separator, and the inside of filter separator is provided with described salt deposit.
2. diesel oil dewatering device according to claim 1, is characterized in that described salt deposit is Industrial Salt.
3. diesel oil dewatering device according to claim 2, is characterized in that described Industrial Salt is sodium-chlor.
4. diesel oil dewatering device according to claim 1, is characterized in that the filtering accuracy of described prefilter is 50-200 micron.
5. diesel oil dewatering device according to claim 1, is characterized in that described coalescent pack layer is coalescent metal, pottery or glass.
6. diesel oil dewatering device according to claim 1, is characterized in that described Coalescence filter core layer is glass fibre, metal, trevira or pottery.
7. diesel oil dewatering device according to claim 1, it is characterized in that described filter separator skin is organic coating, this organic coating is tetrafluoroethylene or vinylidene.
8. diesel oil dewatering device according to claim 1, is characterized in that described prefilter is one or more.
9. diesel oil dewatering device according to claim 1, is characterized in that described coalescing separator is one or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520403674.6U CN205011707U (en) | 2015-06-11 | 2015-06-11 | Diesel oil dewatering device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520403674.6U CN205011707U (en) | 2015-06-11 | 2015-06-11 | Diesel oil dewatering device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205011707U true CN205011707U (en) | 2016-02-03 |
Family
ID=55210321
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520403674.6U Withdrawn - After Issue CN205011707U (en) | 2015-06-11 | 2015-06-11 | Diesel oil dewatering device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205011707U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104893755A (en) * | 2015-06-11 | 2015-09-09 | 洛阳绿景环保科技有限公司 | Diesel oil dehydration device |
| CN108870060A (en) * | 2018-06-27 | 2018-11-23 | 重庆工商大学 | A kind of means of defence of dry type thin oil sealing gas cabinet sealing deterioration of oil |
-
2015
- 2015-06-11 CN CN201520403674.6U patent/CN205011707U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104893755A (en) * | 2015-06-11 | 2015-09-09 | 洛阳绿景环保科技有限公司 | Diesel oil dehydration device |
| CN108870060A (en) * | 2018-06-27 | 2018-11-23 | 重庆工商大学 | A kind of means of defence of dry type thin oil sealing gas cabinet sealing deterioration of oil |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160203 Effective date of abandoning: 20160720 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |