CN202700811U - Pipeline structure of condensing main pipe - Google Patents
Pipeline structure of condensing main pipe Download PDFInfo
- Publication number
- CN202700811U CN202700811U CN 201220322686 CN201220322686U CN202700811U CN 202700811 U CN202700811 U CN 202700811U CN 201220322686 CN201220322686 CN 201220322686 CN 201220322686 U CN201220322686 U CN 201220322686U CN 202700811 U CN202700811 U CN 202700811U
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- Prior art keywords
- condensation
- main pipe
- supervisor
- pipeline
- powder
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Abstract
The utility model relates to a pipeline structure of a condensing main pipe which is arranged obliquely. Powder collectors are arranged at the position of the condensing main pipe. The pipeline structure adopts an obliquely-arranged pipeline of the condensing main pipe, and multi-sectional powder collectors are arranged at the position of the pipeline of the condensing main pipe. Openings of the powder collectors are different in height. The system utilizes the gravity principle of free fall, nano particles with different diameters can fall into different powder collectors, automatic screening and grading of nano particles can be achieved, and the additional value of products is effectively improved. The system is provided with a filtering device, and large-particle raw materials are automatically recycled for regeneration. The production process of the system is short, so that energy consumption is effectively reduced. Compared with the prior art, the pipeline structure of the condensing main pipe has prominent substantive features and obtains remarkable progress.
Description
Technical field
The utility model relates to the technical field of nano particle production system, specifically a kind of condensation supervisor pipeline configuration, particularly its mechanical connecting structure.
Background technology
Documents 1, number of patent application: 201110030665.3, applicant: Tsing-Hua University, the applying date: 2011.01.28, this case discloses " a kind of nano manufacturing system ", comprise that atomic particle produces system, atomic particle produces system and is communicated with source of the gas by valve, atomic particle produces system and is connected with the atom transport system, the atom transport system is connected with vacuum workshop, indoor lifting and the X-Y scheme scanning bracket of placing the nanohole array mask plate that be provided with of vacuum work, top, nanohole array mask plate edge is optical alignment system, nanohole array mask plate below is the nanoscale electric alignment system, and nanohole array mask plate below also is provided with for the substrate multidimensional adjusting pole of laying backing material.
Documents 2, number of patent application: CN200380106661.2, applicant: E. I. Du Pont de Nemours and Co, the applying date: 2003.12.16, this case discloses " utilizing evaporation-condensation process to prepare the method for nano particle by reaction chamber plasma reactor system ", a kind of for the reactor at aerosol process preparation nano particle, comprise: (a) have sidewall, the reative cell of entrance and exit, this entrance is used for heat carrier gas is introduced reative cell, heat carrier gas is from this inlet streams through reative cell and leave this outlet, (b) be positioned at the quench region in reative cell downstream, it has entrance and exit, (c) roughly be positioned near the one or more quenching entrances of reative cell outlet, it is used for introducing quench material, (d) the one or more reactant entrances between reative cell entrance and quenching entrance, it is used for introducing one or more reactants; This reative cell comprises: the spacer region that (i) has length L 1, it begins to extend and roughly stop near reactant entrance from the reative cell entrance, (ii) have the homogenization zone of length L 2, it roughly begins to extend and roughly stop near the quench region entrance from the position of reactant entrance; This spacer region is used for making heat carrier gas that reactant is carried into homogenization zone, this homogenization zone is used for making the reactant contact and product being passed to quench region being suitable for forming under the condition of product, L1 is enough to make heat carrier gas on the sidewall that is attached to the reacting chamber space septal area before the reactant entrance, and L2 is enough to provide the reactant residence time within the homogenization zone, it is suitable for forming such product: when taking out from the quench region outlet, product is nano particle.
Existing nano particle manufacturing system can't be in manufacturing process voluntarily the grade to nano particle carry out sizing screening, can't distinguish the specification of carrying out of product, some bulky grain raw materials can be sneaked in it, cause the grade of product not high, also can't carry out raw materials recovery, cause waste, and the energy consumption of existing system is also larger.
Summary of the invention
The purpose of this utility model is to provide a kind of condensation supervisor pipeline configuration, it is responsible for pipeline with condensation and carries out oblique setting, and at condensation supervisor install pipeline multistage sizing screening powder catcher, utilize the natural gravity principle, realize the automatic screening classification of nano particle, overcome the shortcoming and defect that exists in the prior art.
To achieve these goals, the technical solution of the utility model is: a kind of condensation supervisor pipeline configuration, it comprises the condensation supervisor, it is characterized in that: described condensation supervisor is oblique setting, and the condensation appropriate department is provided with powder catcher.
The utility model discloses a kind of condensation supervisor pipeline configuration; it adopts the condensation supervisor pipeline of oblique setting; and at condensation supervisor pipeline place the multisection type powder catcher is set; the opening of each powder catcher is positioned at different height; the gravity principle of the sharp freely falling body of system; the nano particle of different-diameter can fall in the different powder catchers; realize the classification of nano particle automatic screening; effectively promoted value-added content of product, system carries the large raw material the automatic recovery regeneration of filter ， Teeth grain; the production procedure of system is short; effectively reduce energy consumption, compared to existing technologies, have outstanding substantive distinguishing features and marked improvement.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
The utility model will be further described below in conjunction with drawings and Examples.
The utility model discloses a kind of condensation supervisor pipeline configuration, it comprises condensation supervisor 1, this condensation is responsible for 1 lower end and is connected with plasma reaction still 5 upper ends, and it is different from prior art and is: described condensation supervisor 1 is oblique setting, and condensation is responsible for 1 place and is provided with powder catcher 2.
In the specific implementation, described condensation is responsible for 1 place and is provided with four powder catchers 2, powder catcher 2 is vertical configuration and distributes, and four powder catchers 2 are followed successively by 20 nanometer powder collectors, 40 nanometer powder collectors, 60 nanometer powder collectors, 80 nanometer powder collectors from top to bottom.
In the specific implementation, described condensation supervisor's 1 upper and lower respectively is provided with a temperature probe 3, is used for the temperature regime in the monitoring condensation supervisor pipeline.
In the specific implementation, described condensation is responsible for 1 upper end and is provided with filter 4.
In the specific implementation, described condensation supervisor 1 forms 1 degree to the angle of 89 degree with horizontal plane, and in most preferred embodiment, condensation supervisor 1 forms 30 degree to the angle of 60 degree with horizontal plane.
Above content is in conjunction with concrete preferred embodiment further detailed description of the utility model, can not assert that the utility model implementation is confined to above-mentioned these explanations.For the utility model person of an ordinary skill in the technical field, without departing from the concept of the premise utility, can also make some simple deduction or replace, all should be considered as belonging to protection domain of the present utility model.
Claims (6)
1. pipeline configuration is responsible in a condensation, and it comprises condensation supervisor (1), it is characterized in that: described condensation supervisor (1) is oblique setting, and condensation supervisor (1) locates to be provided with powder catcher (2).
2. pipeline configuration is responsible in a kind of condensation according to claim 1, it is characterized in that: described condensation supervisor (1) locates to be provided with four powder catchers (2), powder catcher (2) is vertical configuration and distributes, and four powder catchers (2) are followed successively by 20 nanometer powder collectors, 40 nanometer powder collectors, 60 nanometer powder collectors, 80 nanometer powder collectors from top to bottom.
3. pipeline configuration is responsible in a kind of condensation according to claim 1, and it is characterized in that: described condensation supervisor's (1) upper and lower respectively is provided with a temperature probe (3).
4. pipeline configuration is responsible in a kind of condensation according to claim 1, it is characterized in that: described condensation supervisor (1) upper end is provided with filter (4).
5. a kind of condensation supervisor pipeline configuration according to claim 1 is characterized in that: described condensation supervisor (1) and the angle of horizontal plane formation 1 degree to 89 degree.
6. a kind of condensation supervisor pipeline configuration according to claim 5 is characterized in that: described condensation supervisor (1) and the angle of horizontal plane formation 30 degree to 60 degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220322686 CN202700811U (en) | 2012-07-05 | 2012-07-05 | Pipeline structure of condensing main pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220322686 CN202700811U (en) | 2012-07-05 | 2012-07-05 | Pipeline structure of condensing main pipe |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202700811U true CN202700811U (en) | 2013-01-30 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220322686 Expired - Fee Related CN202700811U (en) | 2012-07-05 | 2012-07-05 | Pipeline structure of condensing main pipe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202700811U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105382011A (en) * | 2015-12-16 | 2016-03-09 | 华中科技大学 | Handheld powder recycling and packaging system |
-
2012
- 2012-07-05 CN CN 201220322686 patent/CN202700811U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105382011A (en) * | 2015-12-16 | 2016-03-09 | 华中科技大学 | Handheld powder recycling and packaging system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130130 Termination date: 20140705 |
|
| EXPY | Termination of patent right or utility model |