CN210332507U - Flow type integral mixed oil blender - Google Patents

Flow type integral mixed oil blender Download PDF

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Publication number
CN210332507U
CN210332507U CN201920225361.4U CN201920225361U CN210332507U CN 210332507 U CN210332507 U CN 210332507U CN 201920225361 U CN201920225361 U CN 201920225361U CN 210332507 U CN210332507 U CN 210332507U
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China
Prior art keywords
shaped channel
shaped
static mixing
oil
flow
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Expired - Fee Related
Application number
CN201920225361.4U
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Chinese (zh)
Inventor
司维龙
刘延年
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Xinjiang Modo Special Oil Technology Co ltd
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Xinjiang Modo Special Oil Technology Co ltd
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Priority to CN201920225361.4U priority Critical patent/CN210332507U/en
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Abstract

The utility model relates to a whole mixed oil mediation ware of type that flows, its characterized in that includes static mixing trunk line (1, 5), the passageway of falling U-shaped (6) and X-shaped passageway (3), wherein, the passageway of falling U-shaped (6) is located the middle section of static mixing trunk line (5), X-shaped passageway (3) are located the bottom of static mixing trunk line (5), wherein, the passageway of falling U-shaped (6) with be provided with a plurality of spouts mouth (4) on X-shaped passageway (3), wherein, spout mouth (4) and be in unilateral distribution on X-shaped passageway (3), the trompil direction of spout mouth (4) makes mixed oil spout with clockwise. The utility model discloses simple structure is reasonable, make convenient assembling when guaranteeing to mix the effect.

Description

Flow type integral mixed oil blender
Technical Field
The utility model belongs to the technical field of oil industry machine tool, concretely relates to whole mixed oil blending ware of type that flows.
Background
The oil product blending problem solved by the prior art is only simple mixing, the overall mixing degree of the oil product is low, and adverse phenomena such as layering and the like can occur if the standing time is long. For example, the LTHQ dispenser known in the art is connected to the liquid inlet line via an equipment flange, and the dispenser housing has liquid spray nozzles on the side walls and top thereof, so that liquid is sprayed from nozzles uniformly distributed around the dispenser during feeding. The multi-nozzles are divided into 5 and 7 nozzle combinations.
The disadvantage of the above-mentioned prior art dispenser is that the oil is only a preliminary simple blending, even a simple mixing, and the intermolecular mixing of the oil is not considered to be sufficient.
SUMMERY OF THE UTILITY MODEL
In order to compensate prior art not enough, the utility model provides a flow type whole mixed oil mediation ware, its main aim at oil is in the in-process that flows and is advanced the blending tank through the pipeline flow after carrying out a preliminary mixing, and the oil mixes once more in the blending tank for the power is urged jar oil that self carried under the special construction of blending tank in the oil for fully contact misce bene in the oil mediation in-process, makes the oil misce bene when making medium-sized oil transfer, can make the oil wholly flow the state good.
According to the embodiment of the utility model, a flow type whole mixed oil mediation ware is provided, its characterized in that includes static mixing trunk line, the passageway of falling the U-shaped and X-shaped passageway, wherein, the passageway of falling the U-shaped is located static mixing trunk line back end, X-shaped passageway is located the bottom of static mixing trunk line, wherein, the passageway of falling the U-shaped with be provided with a plurality of spouts mouth on the X-shaped passageway, wherein, the spout mouth is in unilateral distribution on the X-shaped passageway, the trompil direction of spout mouth makes mixed oil spout with clockwise or anticlockwise.
According to the utility model discloses an embodiment, the inner wall laminating of static mixed trunk line anterior segment has the drainage folded plate, the drainage folded plate is the spiral distortion shape.
According to the utility model discloses an embodiment, the inverted U-shaped passageway is 2 branches or 4 branch shapes.
According to the utility model discloses an embodiment, static mixed trunk line anterior segment is connected with the tee bend for introduce different oils respectively.
According to the utility model discloses an embodiment, the type that flows whole mixed oil blending ware is installed in the blending tank top, the X-shaped passageway is 50 centimetres apart from the tank bottoms, wherein, static state mixing trunk line is
Figure BDA0001976301280000021
Or
Figure BDA0001976301280000023
The inverted U-shaped channel and the X-shaped channel may be
Figure BDA0001976301280000022
Of 2 meters each of the 4 branches of the X-shaped channel.
The beneficial effects of the utility model include: the structure is simple and reasonable, the manufacture and the assembly are convenient, and the target object can be fixed to the maximum extent under the condition that the object is not damaged, namely, the object can bear the action of larger force without the phenomenon that the target object falls off.
Drawings
FIG. 1 is a schematic diagram illustrating a front section of a flow-type bulk hybrid oil blender according to an embodiment of the present invention;
fig. 2 is a rear-end structural schematic diagram illustrating a flow-type integrated mixed oil blender according to an embodiment of the present invention.
List of reference numerals:
static mixing part: 1. a front section of a static mixing main pipeline; 2. drainage folded plates; 5. a back section of the static mixing main pipeline; 6. an inverted U-shaped channel; 3. an X-shaped channel; 4. and a jet flow port.
Detailed Description
The following describes the embodiments in further detail with reference to the accompanying drawings.
It will be appreciated by those skilled in the art that while the following description refers to numerous technical details relating to embodiments of the present invention, this is by way of example only, and not by way of limitation, to illustrate the principles of the invention. The present invention can be applied to other fields than the technical details exemplified below as long as they do not depart from the principle and spirit of the present invention.
In addition, in order to avoid limiting the description of the present specification to a great extent, in the description of the present specification, it is possible to omit, simplify, and modify some technical details that may be obtained in the prior art, as would be understood by those skilled in the art, and this does not affect the sufficiency of disclosure of the present specification.
The following describes in detail the preferred embodiments of the present invention with reference to the accompanying drawings.
FIG. 1 is a schematic diagram illustrating a front section of a flow-type bulk hybrid oil blender according to an embodiment of the present invention; fig. 2 is a rear-end structural schematic diagram illustrating a flow-type integrated mixed oil blender according to an embodiment of the present invention.
As shown in fig. 1, according to the utility model discloses an inner wall laminating of the static mixing trunk line anterior segment 1 of the whole mixed oil mediation ware anterior segment of type that flows has drainage folded plate 2, drainage folded plate 2 is spiral distortion shape, for example, twists into this shape through the instrument with the band iron that thickness is 3mm, then welds it on the inner wall of static mixing trunk line anterior segment 1.
As shown in fig. 2, according to the utility model discloses a static mixing trunk line back end 5 that the whole mixed oil mediation ware back end of type that flows is of embodiment does not set up drainage folded plate 2, and the upper end intercommunication of static mixing trunk line back end 5 has the passageway 6 of falling the U-shaped, and the lower extreme intercommunication of static mixing trunk line back end 5 has X shape passageway 3, the passageway 6 of falling the U-shaped with a plurality of spouts mouth 4 have been arranged on the X shape passageway 3.
For example, the main static mixing conduit may be
Figure BDA0001976301280000031
Or
Figure BDA0001976301280000032
The pipe of (1). The inverted U-shaped channel 6 and the X-shaped channel 3 may be
Figure BDA0001976301280000033
The pipe of (1). The length of each branch in 4 branches of the X-shaped channel 3 is 2 meters, and the jet flow ports 4 are through holes which are uniformly distributed at intervals of 5 centimeters. Wherein, as an example, the jet ports 4 are distributed on one side of the X-shaped channel 3, and the opening direction of the jet ports 4 enables the mixed oil to jet in a clockwise or counterclockwise direction.
Optionally, the inverted U-shaped channel 6 is 2-branched or 4-branched.
Similarly, the jet ports 4 are distributed on one side of the inverted U-shaped channel 6, and the opening direction of the jet ports 4 enables mixed oil to jet in a clockwise direction or a counterclockwise direction.
In use, the oil product blender is arranged at the top of a blending tank (not shown), the distance between the X-shaped channel and the inner wall of the tank bottom can be ensured to be 50cm, the front section 1 of the static mixing main pipeline is connected with a tee joint, and two ends of the static mixing main pipeline are respectively fed with two oil products to be blended.
When the difference between the two oil products is large, the oil product with small requirement amount firstly enters the oil product blender to enter the blending tank, and the oil product with large requirement amount subsequently enters the blending tank to be well blended under the special structure of the oil product blender.
The final effect achieved by the arrangement direction of the jet flow ports 4 is that the whole liquid in the tank is in a clockwise or anticlockwise flowing state so as to achieve the aim of oil product blending. That is, the spout mouth design is for evenly distributed on one side of the pipeline, can the flow of effectual drive oil, and the distribution of the pipeline of falling the U-shaped and X-shaped fully considers jar synchronous circulation drive upper portion oil circulation of internal portion oil lower part and middle part for the oil of whole jar internal portion presents the mixture of mobile state.
The invention has simple manufacturing method and low cost, leads the oil product to be mixed more evenly and fully, and is very practical, convenient and quick in operation.
Finally, those skilled in the art will appreciate that various modifications, adaptations, and alternatives can be made to the above-described embodiments of the present invention, all falling within the scope of the invention as defined by the appended claims.

Claims (5)

1. A flow type integral mixed oil blender is characterized by comprising a static mixed main pipeline, an inverted U-shaped channel (6) and an X-shaped channel (3),
wherein the static mixing main pipeline comprises a front section (1) of the static mixing main pipeline and a rear section (5) of the static mixing main pipeline,
wherein the inverted U-shaped channel (6) is positioned at the rear section (5) of the static mixing main pipeline, the X-shaped channel (3) is positioned at the bottom end of the static mixing main pipeline,
wherein a plurality of jet ports (4) are arranged on the inverted U-shaped channel (6) and the X-shaped channel (3),
the jet flow ports (4) are distributed on one side of the X-shaped channel (3), and the opening direction of the jet flow ports (4) enables mixed oil to jet in a clockwise or anticlockwise direction.
2. The flow-type integrated mixing oil blender as claimed in claim 1, wherein the inner wall of the front section (1) of the static mixing main pipe is adhered with a diversion flap (2), and the diversion flap (2) is in a spiral twisted shape.
3. The flow-type integrated mixing oil conditioner according to claim 2, characterized in that said inverted U-shaped channel (6) is 2-or 4-branch shaped.
4. The flow-type integrated mixed oil blender as claimed in claim 1, wherein the static mixing main pipe front section (1) is connected with a tee for introducing different oil products respectively.
5. The flow-type integrated mixing oil conditioner according to any one of claims 1 to 4, characterized in that it is installed on top of a mixing tank, said X-shaped channel (3) being 50cm from the bottom of the tank,
wherein the static mixing main pipeline is
Figure FDA0001976301270000011
Or
Figure FDA0001976301270000012
The inverted U-shaped channel (6) and the X-shaped channel (3) are
Figure FDA0001976301270000013
Of the X-shaped channel (3), each of the 4 branches of the X-shaped channel having a length of 2 meters.
CN201920225361.4U 2019-02-22 2019-02-22 Flow type integral mixed oil blender Expired - Fee Related CN210332507U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920225361.4U CN210332507U (en) 2019-02-22 2019-02-22 Flow type integral mixed oil blender

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920225361.4U CN210332507U (en) 2019-02-22 2019-02-22 Flow type integral mixed oil blender

Publications (1)

Publication Number Publication Date
CN210332507U true CN210332507U (en) 2020-04-17

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920225361.4U Expired - Fee Related CN210332507U (en) 2019-02-22 2019-02-22 Flow type integral mixed oil blender

Country Status (1)

Country Link
CN (1) CN210332507U (en)

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Granted publication date: 20200417

CF01 Termination of patent right due to non-payment of annual fee