CN205120195U - Large -traffic poor two -phase fluid's of non - mixed phase volume metering device - Google Patents

Large -traffic poor two -phase fluid's of non - mixed phase volume metering device Download PDF

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Publication number
CN205120195U
CN205120195U CN201520872952.2U CN201520872952U CN205120195U CN 205120195 U CN205120195 U CN 205120195U CN 201520872952 U CN201520872952 U CN 201520872952U CN 205120195 U CN205120195 U CN 205120195U
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section
cock
measuring device
measurer
fluid
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左丽丽
崔轩榕
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China University of Petroleum Beijing
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China University of Petroleum Beijing
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Abstract

The utility model relates to a large -traffic poor two -phase fluid's of non - mixed phase volume metering device, it includes a measurer and an iron stand platform that is used for supporting the measurer, the measurer is including being integrative major diameter measuring section and the minor diameter measuring section that sets up, and the major diameter measuring section is coaxial setting and inside intercommunication with the minor diameter measuring section, import and export at the tip of minor diameter measuring section and be provided with a first cock, import and export at the tip of major diameter measuring section and be provided with a second cock. The utility model discloses can / little different situation big through low discharge fluid density in two kinds of fluids of position relation reply of the transform big diameter section of measurer and little diameter section, in measurement process, hold the less fluid of flow with little diameter section all the time, avoided measuring the error that the low discharge fluid causes with the large capacity measurer, on the other hand emits partly fluidic mode messenger measurement liquid level and remains throughout in the measurer among the measurement process, avoided the change error that the measurer brought, consequently, the utility model discloses the measurement that realizes is more accurate.

Description

A kind of volume metering mechanism of non-mixed phase large discharge difference two-phase fluid
Technical field
The utility model relates to a kind of measuring apparatus, is specifically related to a kind of volume metering mechanism of non-mixed phase large discharge difference two-phase fluid.
Background technology
In oil and gas development in-house laboratory investigation and produced on-site, the situation that two kinds of fluids (such as crude oil and water) of the non-mixed phase of frequent appearance flow in same pipeline or porous medium, the metering for these fluid volumes or flow generally adopts the vessel such as graduated cylinder or beaker.If the flow of these two kinds of fluids relatively, then this metering vessel are feasible.If but the flow difference of two kinds of fluids is very large, such as, in oil displacement experiment, (oil phase flow is increasing for the process of saturated oil, aqueous phase flow is more and more less) and water displacing oil process (aqueous phase flow is increasing, oil phase flow is more and more less), when measuring with this graduated cylinder or beaker again, just may occur that two kinds cause measuring coarse situation, if the first vessel of low capacity measure, then vessel are easily full, need often to change, increase experiment difficulty and error in dipping; If measure with jumbo vessel, then for the fluid that flow is little, measuring accuracy is inadequate.Therefore, design a kind of can the device of the larger two-phase fluid volume of accurate measurement flow difference very necessary.
Summary of the invention
For the problems referred to above, the purpose of this utility model is to provide the volume metering mechanism of the high non-mixed phase large discharge difference two-phase fluid of a kind of measuring accuracy.
For achieving the above object, the utility model by the following technical solutions: a kind of volume metering mechanism of non-mixed phase large discharge difference two-phase fluid, is characterized in that: it comprises a measuring device and for supporting the iron stand of described measuring device; Described measuring device comprises large diameter measurement section in being wholely set and minor diameter measuring section, and described large diameter measurement section and described minor diameter measuring section to be arranged and inside is communicated with in coaxial; On the end of described minor diameter measuring section is imported and exported, be provided with one first cock, on the end of described large diameter measurement section is imported and exported, be provided with one second cock.
Described measuring device with described reduced diameter section upper, described enlarged diameter section under mode vertical support on described iron stand, place a graduated cylinder being positioned at the described iron stand below described measuring device.
Described measuring device with described enlarged diameter section upper, described reduced diameter section under mode vertical support on described iron stand; Described second cock is provided with a vertical through hole and an oblique perforate be communicated with described vertical through hole, in described oblique perforate, inserts a piston; The described iron stand being positioned at described enlarged diameter section side supports a graduated cylinder, and the opening of described graduated cylinder exports relative with the described oblique through hole of described second cock.
Described measuring device is made up of transparent material, and the described enlarged diameter section and reduced diameter section of described measuring device are carved with scale mark respectively.
Described first cock, the second cock and piston are frosted plug.
The utility model is owing to taking above technical scheme, it has the following advantages: 1, the utility model can tackle large/little different situations of two kinds of fluid medium-small flow fluid densities by the position relationship of conversion measuring device enlarged diameter section and reduced diameter section, in metering process, all the time the less a kind of fluid of flow is held with reduced diameter section, avoid the error caused with Large Copacity measuring device measurement low discharge fluid, on the other hand, the mode of releasing a part of fluid in metering process makes measurement liquid level remain in measuring device, avoid the error changed measuring device and bring, therefore, the measurement that the utility model realizes is more accurate.2, measuring device of the present utility model is made up of transparent material, and is carved with scale mark respectively on enlarged diameter section and reduced diameter section, is convenient to observe in experimentation.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the utility model under the first use-pattern;
Fig. 2 is the schematic diagram of the utility model in second under use-pattern;
Fig. 3 is the structural representation of the utility model second cock.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in detail.
As shown in Figure 1 and Figure 2, the utility model comprises a measuring device 1 and for supporting the iron stand 2 of measuring device 1.Measuring device 1 comprises large diameter measurement section 11 in being wholely set and minor diameter measuring section 12, and wherein, large diameter measurement section 11 and minor diameter measuring section 12 to be arranged and inside is communicated with in coaxial.On the end of minor diameter measuring section 12 is imported and exported, be provided with one first cock 3, on the end of large diameter measurement section 11 is imported and exported, be provided with one second cock 4.First cock 3 adopts the cock with a vertical through hole in prior art; Second cock 4, on the basis arranging vertical through hole, sets up an oblique perforate be communicated with vertical through hole, and in oblique perforate, insert a piston 5 (as shown in Figure 3).
In above-described embodiment, as shown in Figure 1, measuring device 1 can with reduced diameter section 12 upper, enlarged diameter section 11 under mode vertical support on iron stand 2, and place a graduated cylinder 6 at the iron stand 2 be positioned at below measuring device 1, set-up mode is now applicable in fluid to be batched, the situation (hereafter will describe in detail) that the fluid density that flow is little is also less.
In above-described embodiment, as shown in Figure 2, measuring device 1 also can with enlarged diameter section 11 upper, reduced diameter section 12 under mode vertical support on iron stand 2, the oblique through hole of the second cock 4 is the direction placement of lower-left upper right, and on the iron stand 2 being positioned at enlarged diameter section 11 side, support a graduated cylinder 6, the opening of graduated cylinder 6 exports relative with the oblique through hole of the second cock 4, set-up mode is now applicable in fluid to be batched, the situation (hereafter will describe in detail) that the fluid density that flow is little is larger.
In above-described embodiment, enlarged diameter section 11 and reduced diameter section 12 also can be processed respectively, are then tightly connected by rubber plug etc., and its advantage is to combine according to demand, but also there is the problem that difficulty of processing is large, cost is high, error increases.
In above-described embodiment, measuring device 1 can be made up of transparent material, and is carved with scale mark respectively on enlarged diameter section 11 and reduced diameter section 12, is convenient to the observation in experimentation.
In above-described embodiment, the first cock 3, second cock 4 and piston 5 are frosted plug.
The utility model in use, can be divided into two kinds of situations:
(1) situation one: the fluid density that flow is little is less.As shown in Figure 1, the reduced diameter section 12 of measuring device 1 is arranged on the top of enlarged diameter section 11 in use, need for keeping accurate measurement in enlarged diameter section 11, be full of that large one phase flow body of density in advance, then the first cock 3 is opened, two-phase fluid is imported and exported from the end of reduced diameter section 12 and is flowed into, and can start metering.When fluid will be full of reduced diameter section 12, open the second cock 4 (piston 5 in the second cock 4 is in sealing state), the fluid inflow cylinder 6 in metering, liquid level in reduced diameter section 12 declines, close the second cock 4 after stable, continue reading, so carry out subsequent experimental.
(2) situation two: the fluid density that flow is little is larger.As shown in Figure 2, the reduced diameter section 12 of measuring device 1 is arranged on the below of enlarged diameter section 11 in use.Close the first cock 3, open the second cock 4, two-phase fluid metering from the end of enlarged diameter section 11 is imported and exported after inflow.When two-phase fluid is full of measuring device 1, can pull out the piston 5 in the second cock 4, unnecessary fluid can flow into graduated cylinder 6, and experiment can proceed.If graduated cylinder 6 is not easily placed, also can pass through the afterbody connection rubber tube in the second cock 4 and extend to groove 7 place, the other one section of access graduated cylinder 6 of rubber tube.If the fluid that density is larger is full of reduced diameter section 12, then open the first cock, release a part of fluid to (should be the graduated cylinder that precision is higher) in graduated cylinder, treat the follow-up number of resuming studies of liquid level stabilizing, so carry out subsequent experimental.
Utilize the utility model, the maximum volume of quantifiable low discharge fluid is the volume sum of large diameter measurement section 11 and minor diameter measuring section 12, all meterings within the scope of this, all by regulating the first cock 3 or the second cock 4 to realize, the volume of the phase that flow is large can carry out submeter by external graduated cylinder 6.
The utility model is only described with above-described embodiment, and the structure of each parts, setting position and connection thereof all can change to some extent.On the basis of technical solutions of the utility model, all improvement of carrying out individual part according to utility model principle of the present utility model or equivalents, all should not get rid of outside protection domain of the present utility model.

Claims (6)

1. a volume metering mechanism for non-mixed phase large discharge difference two-phase fluid, is characterized in that: it comprises a measuring device and for supporting the iron stand of described measuring device; Described measuring device comprises large diameter measurement section in being wholely set and minor diameter measuring section, and described large diameter measurement section and described minor diameter measuring section to be arranged and inside is communicated with in coaxial; On the end of described minor diameter measuring section is imported and exported, be provided with one first cock, on the end of described large diameter measurement section is imported and exported, be provided with one second cock.
2. the volume metering mechanism of a kind of non-mixed phase large discharge difference two-phase fluid as claimed in claim 1, it is characterized in that: described measuring device with described reduced diameter section upper, described enlarged diameter section under mode vertical support on described iron stand, place a graduated cylinder being positioned at the described iron stand below described measuring device.
3. the volume metering mechanism of a kind of non-mixed phase large discharge difference two-phase fluid as claimed in claim 1, is characterized in that: described measuring device with described enlarged diameter section upper, described reduced diameter section under mode vertical support on described iron stand; Described second cock is provided with a vertical through hole and an oblique perforate be communicated with described vertical through hole, in described oblique perforate, inserts a piston; The described iron stand being positioned at described enlarged diameter section side supports a graduated cylinder, and the opening of described graduated cylinder exports relative with the described oblique through hole of described second cock.
4. the volume metering mechanism of a kind of non-mixed phase large discharge difference two-phase fluid as described in claim 1 or 2 or 3, is characterized in that: described measuring device is made up of transparent material, the described enlarged diameter section and reduced diameter section of described measuring device is carved with scale mark respectively.
5. the volume metering mechanism of a kind of non-mixed phase large discharge difference two-phase fluid as described in claim 1 or 2 or 3, is characterized in that: described first cock, the second cock and piston are frosted plug.
6. the volume metering mechanism of a kind of non-mixed phase large discharge difference two-phase fluid as claimed in claim 4, is characterized in that: described first cock, the second cock and piston are frosted plug.
CN201520872952.2U 2015-11-04 2015-11-04 Large -traffic poor two -phase fluid's of non - mixed phase volume metering device Active CN205120195U (en)

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Application Number Priority Date Filing Date Title
CN201520872952.2U CN205120195U (en) 2015-11-04 2015-11-04 Large -traffic poor two -phase fluid's of non - mixed phase volume metering device

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109900855A (en) * 2017-12-07 2019-06-18 中国石油化工股份有限公司 For evaluating the experimental provision and method of easily hydrated clay or drilling fluid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109900855A (en) * 2017-12-07 2019-06-18 中国石油化工股份有限公司 For evaluating the experimental provision and method of easily hydrated clay or drilling fluid

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