CN205925025U - Grease leaches course of working and uses first evaporimeter - Google Patents
Grease leaches course of working and uses first evaporimeter Download PDFInfo
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- CN205925025U CN205925025U CN201620889824.3U CN201620889824U CN205925025U CN 205925025 U CN205925025 U CN 205925025U CN 201620889824 U CN201620889824 U CN 201620889824U CN 205925025 U CN205925025 U CN 205925025U
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- miscella
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- separation chamber
- end socket
- solvent
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Abstract
The utility model provides a grease leaches course of working and uses first evaporimeter, including a tub case, body and separation chamber, the pipe case is in the bottom, and the body is on tub case, and the separation chamber is on the body, and this three part equal two dual -purpose bolted connection get up. The utility model discloses can be in the miscella evaporation process that the grease leached, next solvent - the water steam mix gas of will discharging is used as the heat source and evaporates the most solvent in the miscella in the shell side, the separation chamber is direct coaxial vertical continuous with the body, the miscella and the solvent vapo(u)r level of revolving after the liquid volute will evaporate in the separation chamber are got rid of to the outer wall, liquid gets into the shell side of crude oil / miscella heat exchanger downwards because of gravity, solvent gas is constantly inhaleed in the evaporation -condensation ware, make the evaporimeter maintain its high vacuum, miscella and solvent vapo(u)r are fully separated.
Description
Technical field
This utility model is related to a kind of oil extraction course of processing the first vaporizer.
Background technology
In the technical process of oil extraction, the evaporation of miscella and stripping are one of oil extraction production important rings
Section, it plays decisive action to the solvent consumption in the quality and leaching production of Extractive crudeoil.And mix oil processing consumed molten
The ratio that dosage accounts for whole leaching production solvent consumption is very big, therefore, on the premise of solvent in effective removing miscella, maximum
Degree ground reduces solvent-oil ratio, attention in miscella treatment process.At present in commercial production, oils and fatss miscella evaporation
Consume very greatly with stripping solvent, the solvent of use does not all account for recycling, to production cost, working condition and environmental conservation
Unfavorable.
Utility model content
The utility model proposes a kind of oil extraction course of processing the first vaporizer, using solvent vapor gaseous mixture
The waste-heat miscella of body, makes mixed gas turn waste into wealth, material is fully used, and meets energy-saving and emission-reduction, low-carbon environment-friendly,
The up-to-date trend of our times.
The technical solution of the utility model is realized in：
A kind of oil extraction course of processing the first vaporizer, includes bobbin carriage 1, body 2 and separation chamber 3, bobbin carriage is
Below, on bobbin carriage 1, on body 2, these three parts are all connected with body 2 two-by-two for separation chamber 3, and it is special
Levy and be：
Described bobbin carriage 1 is made up of miscella inlet tube 1-1 and ellipse end socket 1-2, and wherein miscella inlet tube 1-1 pacifies
It is contained in the bottom of ellipse end socket 1-2；
Described body 2 is by condensate outlet pipe 2-1, mixed gas outlet assembly 2-2, ear mount 2-3, heat exchanger tube 2-4, baffling
Plate 2-5, pull bar 2-6, shell 2-7, combi inlet port assembly 2-8 and clean-up port 2-9 composition, wherein condensate outlet pipe 2-1 and
Mixed gas outlet assembly 2-2 is arranged on the bottom of shell 2-7, and heat exchanger tube 2-4 and pull bar 2-6 is arranged on through deflection plate 2-5
In shell 2-7, ear mount 2-3 is welded on the bottom of shell 2-7, and combi inlet port assembly 2-8 is arranged on the top of shell 2-7, clearly
Reason mouth 2-9 is arranged on shell 2-7；
Described separation chamber 3 by miscella inlet tube 3-1, spinning liquid volute 3-2, housing 3-3, man-hole opening and mirror mouth 3-4,
Hanger 3-5, solvent vapor outlet pipe 3-6, miscella outlet partition plate 3-7 and miscella outlet 3-8 composition, wherein mix oil inlet
Pipe 3-1 is arranged on the lower ellipse end socket of housing 3-3, and spinning liquid volute 3-2 is arranged on the top of miscella inlet tube 3-1, people
Aperture and mirror mouth 3-4 are welded on circular shell 3-3, and solvent vapor outlet pipe 3-6 is arranged on the upper ellipse end socket of housing 3-3
On, miscella outlet partition plate 3-7 is welded in the lower ellipse end socket of housing 3-3, and miscella outlet 3-8 is arranged on housing 3-
On 3 lower ellipse end socket.
Preferably, the outer surface of described body 2 is additionally provided with adiabator layer, makes the first vaporizer have good adiabatic effect
Really.
Preferably, the miscella inlet tube 3-1 of described separation chamber 3 is directly coaxially vertically connected so that two with body 2
Part is organically combined, and steadily reliability is supported by body.
What this utility model produced has the beneficial effect that：This utility model can be in the miscella evaporation process of oil extraction
In, the solvent ejecting vapor mixed gas are used as the major part that thermal source to evaporate in miscella in shell side molten
Agent, separation chamber is directly coaxially vertically connected with body, separates indoor spinning liquid volute by the miscella after evaporating and solvent vapo(u)r
Level gets rid of outer wall, and liquid is downwardly into the shell side of crude oil/mixing oil heat exchanger because of gravity, and solvent gas are constantly inhaled into evaporation
In condenser, vaporizer is made to maintain its fine vacuum, miscella and solvent vapo(u)r to be sufficiently separated, therefore its evaporation effect
Well, there is solvent-oil ratio low, solvent recovering rate is high, Extractive crudeoil residual solvent is low, improves product quality, improves work
Condition, reduces the pollution to environment, combines evaporation and separation, operation is easier simultaneously, saves equipment and materials and uses
Amount, structure is more rationally advanced.
Brief description
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or in description of the prior art the accompanying drawing of required use be briefly described it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Specific embodiment
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely description is it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under the premise of making creative work
The every other embodiment being obtained, broadly falls into the scope of this utility model protection.
A kind of oil extraction course of processing the first vaporizer, includes bobbin carriage 1, body 2 and separation chamber 3 as shown in Figure 1,
In bottom, on bobbin carriage 1, on body 2, these three parts have all been connected with body 2 bobbin carriage two-by-two for separation chamber 3
Come, described bobbin carriage 1 is made up of miscella inlet tube 1-1 and ellipse end socket 1-2, and wherein miscella inlet tube 1-1 is arranged on
The bottom of ellipse end socket 1-2；Described body 2 by condensate outlet pipe 2-1, mixed gas outlet assembly 2-2, ear mount 2-3, change
Heat pipe 2-4, deflection plate 2-5, pull bar 2-6, shell 2-7, combi inlet port assembly 2-8 and clean-up port 2-9 composition, wherein condensed fluid
Outlet 2-1 and mixed gas outlet assembly 2-2 is arranged on the bottom of shell 2-7, and heat exchanger tube 2-4 and pull bar 2-6 passes through deflection plate
2-5 is arranged in shell 2-7, and ear mount 2-3 is welded on the bottom of shell 2-7, and combi inlet port assembly 2-8 is arranged on shell 2-
7 top, clean-up port 2-9 is arranged on shell 2-7；Described separation chamber 3 by miscella inlet tube 3-1, spinning liquid volute 3-2,
Housing 3-3, man-hole opening and mirror mouth 3-4, hanger 3-5, solvent vapor outlet pipe 3-6, miscella outlet partition plate 3-7 and miscella go out
Mouth pipe 3-8 composition, wherein miscella inlet tube 3-1 is arranged on the lower ellipse end socket of housing 3-3, and spinning liquid volute 3-2 installs
At the top of miscella inlet tube 3-1, man-hole opening and mirror mouth 3-4 are welded on circular shell 3-3, solvent vapor outlet pipe 3-6
It is arranged on the upper ellipse end socket of housing 3-3, miscella outlet partition plate 3-7 is welded in the lower ellipse end socket of housing 3-3,
Miscella outlet 3-8 is arranged on the lower ellipse end socket of housing 3-3.
The outer surface of the body 2 described in the present embodiment is additionally provided with adiabator layer, so that the first vaporizer is had good exhausted
Thermal effect.
The miscella inlet tube 3-1 of the separation chamber 3 described in the present embodiment be directly coaxially vertically connected with body 2 so that
Two parts are organically combined, and steadily reliability is supported by body.
During work, the solvent vapor mixed gas ejecting enter the first vaporizer by combi inlet port assembly
In shell side, mixed gas Tortuous flow between the deflection plate in shell side is conducted heat, after condensing further in shell side, from mixing
Gas spout assembly flows out in water distributing can, is entered by miscella inlet tube from the miscella of crude oil stripper and solvent vapo(u)r
Enter in the tube side of the first vaporizer, heated in tube side, after heating, miscella and solvent vapo(u)r rise to and separate indoor quilt
Level gets rid of outer wall, and liquid is downwardly into the shell side of crude oil/mixing oil heat exchanger because of gravity, and solvent gas are constantly inhaled into evaporation
In condenser.
This utility model provides a kind of efficient, energy-conservation novel device in the miscella evaporation technique of oil extraction, makes oil
The mixed gas heating miscella discharged in fat extract technology, improves the temperature of miscella, so that miscella and solvent vapo(u)r is obtained
To being sufficiently separated, save the energy, so that mixed gas is turned waste into wealth, material is fully used simultaneously, thus effectively eliminating
Gaseous mixture discharge in extract technology, reduces production cost, improves working condition, reduce the pollution to environment.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model, all this
Within the spirit of utility model and principle, any modification, equivalent substitution and improvement made etc., should be included in this utility model
Protection domain within.
Claims (3)
1. a kind of oil extraction course of processing the first vaporizer, includes bobbin carriage (1), body (2) and separation chamber (3), bobbin carriage
(1) in bottom, body (2) on bobbin carriage (1), separation chamber (3) on body (2), the equal two dual-purpose spiral shells of these three parts
Bolt couple together it is characterised in that：
Described bobbin carriage (1) is made up of miscella inlet tube (1-1) and ellipse end socket (1-2), wherein miscella inlet tube (1-
1) it is arranged on the bottom of ellipse end socket (1-2)；
Described body (2) is by condensate outlet pipe (2-1), mixed gas outlet assembly (2-2), ear mount (2-3), heat exchanger tube (2-
4), deflection plate (2-5), pull bar (2-6), shell (2-7), combi inlet port assembly (2-8) and clean-up port (2-9) composition, wherein
Condensate outlet pipe (2-1) and mixed gas outlet assembly (2-2) are arranged on bottom, heat exchanger tube (2-4) and the pull bar of shell (2-7)
(2-6) all it is arranged in shell (2-7) through deflection plate (2-5), ear mount (2-3) is welded on the bottom of shell (2-7), gaseous mixture
Import assembly (2-8) is arranged on the top of shell (2-7), and clean-up port (2-9) is arranged on shell (2-7)；
Described separation chamber (3) is by miscella inlet tube (3-1), spinning liquid volute (3-2), housing (3-3), man-hole opening and mirror mouth
(3-4), hanger (3-5), solvent vapor outlet pipe (3-6), miscella outlet partition plate (3-7) and miscella outlet (3-8) composition,
Wherein miscella inlet tube (3-1) is arranged on the lower ellipse end socket of housing (3-3), and spinning liquid volute (3-2) is arranged on mixing
The top of oil inlet pipe (3-1), man-hole opening and mirror mouth (3-4) are welded on circular shell (3-3), solvent vapor outlet pipe (3-
6) it is arranged on the upper ellipse end socket of housing (3-3), miscella outlet partition plate (3-7) is welded on the lower ellipse of housing (3-3)
In type end socket, miscella outlet (3-8) is arranged on the lower ellipse end socket of housing (3-3).
2. as claimed in claim 1 a kind of oil extraction course of processing with the first vaporizer it is characterised in that：Described body
(2) outer surface is additionally provided with adiabator layer, makes the first vaporizer have good insulation effect.
3. as claimed in claim 1 a kind of oil extraction course of processing with the first vaporizer it is characterised in that：Described separation
The miscella inlet tube (3-1) of room (3) be directly coaxially vertically connected with body (2) so that two parts organically group is combined in one
Rise, steadily reliability is supported by body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620889824.3U CN205925025U (en) | 2016-08-16 | 2016-08-16 | Grease leaches course of working and uses first evaporimeter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620889824.3U CN205925025U (en) | 2016-08-16 | 2016-08-16 | Grease leaches course of working and uses first evaporimeter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205925025U true CN205925025U (en) | 2017-02-08 |
Family
ID=57917922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620889824.3U Active CN205925025U (en) | 2016-08-16 | 2016-08-16 | Grease leaches course of working and uses first evaporimeter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205925025U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108373945A (en) * | 2018-04-28 | 2018-08-07 | 湖南淳湘农林科技有限公司 | A kind of miscella evaporation device |
| CN110947192A (en) * | 2019-12-02 | 2020-04-03 | 大连海事大学 | Vertical energy-saving evaporator |
-
2016
- 2016-08-16 CN CN201620889824.3U patent/CN205925025U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108373945A (en) * | 2018-04-28 | 2018-08-07 | 湖南淳湘农林科技有限公司 | A kind of miscella evaporation device |
| CN110947192A (en) * | 2019-12-02 | 2020-04-03 | 大连海事大学 | Vertical energy-saving evaporator |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |