CN101357318B - Bridge type pump reactor - Google Patents
Bridge type pump reactor Download PDFInfo
- Publication number
- CN101357318B CN101357318B CN2008101418940A CN200810141894A CN101357318B CN 101357318 B CN101357318 B CN 101357318B CN 2008101418940 A CN2008101418940 A CN 2008101418940A CN 200810141894 A CN200810141894 A CN 200810141894A CN 101357318 B CN101357318 B CN 101357318B
- Authority
- CN
- China
- Prior art keywords
- pump
- reactor
- function
- bridge
- mechanical pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Abstract
The invention discloses a bridge pump reactor which takes a pump as a main reaction apparatus and has reaction function and delivering function. The apparatus comprises a mechanical pump (1), at least a jet pump (3) which is bridged to the two ends of an inlet and an outlet of the mechanical pump by a pipe to form a bridge type reflux, a discharge hole is connected with the outlet end of the mechanical pump (1), and a feeding hole is connected with a negative pressure hole of the jet pump (3). The pump reactor is characterized in that the pump is taken as the main reaction apparatus and caused to have the high-efficiency reaction function and the delivering function, therefore, the efficiency of the reactor is maximized. In the method, the pump which is conventionally regarded as a conveyor is used as a reactor, therefore, in addition to the original conveyor function of the pump, and the potential reactor function of the pump is fully developed, therefore, a completely new and high-efficiency reactor is provided. The reactor only consists of the pump and the pipe, therefore, the structure of the bridge pump reactor is simple and the reactor is easy to be operated.
Description
Technical field
The present invention relates to that fluid is carried and consersion unit, relate in particular to a kind of with pump as the key reaction apparatus, have the reactor of response function and conveying function simultaneously.
Background technology
Now, all kinds of pumps are widely used as and are conveying equipment for fluid substances, and it is subjected to the limitation of self aufbauprinciple, have transport loss power factor (PF)s such as friction, turbulent flow in the pump housing unavoidablely, wherein especially with jet pump for very, its transmission power loss is generally up to more than 60%.But observe from the angle of reactor, external energy can be converted into inner high-intensity turbulent flow of medium and friction rapidly, just its reaction effective power factor.Therefore, jet pump often is applied in the reactor assembly, for example, disclosed technology contents in the Chinese patent ZL200510021057.0 reactive material generation rapid-action method, mechanical pump in this patent serves as conveying equipment, only brought into play the conveying effect, the reaction effect of its inherence is wasted.
Summary of the invention
The present invention will solve that existing fluid delivery pump has only been brought into play the conveying effect and the effect of performance reaction preferably technical problem, propose a kind of with pump as the key reaction apparatus, have the bridge type pump reactor of highly effective reaction function and conveying function simultaneously.
For addressing the above problem, technical scheme of the present invention is a kind of bridge type pump reactor of structure, and it comprises that a mechanical pump, at least one jet pump form the bridge-type backflow by the pipeline cross-over connection of diameter optimization in the import and export two ends of this mechanical pump.The port of export of described mechanical pump is connected with discharging opening, and the negative pressure mouth of described jet pump connects charging aperture.
Preferred version of the present invention, described jet pump is selected many, and it forms bridge-type by pipeline series connection and/or cross-over connection in parallel and refluxes in the import and export two ends of described mechanical pump.
Wherein, also be provided with return valve on the pipeline of described mechanical pump outlet, described discharging opening is connected with the discharging valve, and the charging aperture of described jet pump is connected with the charging valve.
Also be provided with the startup valve on the pipeline of described mechanical pump import.
The present invention forms bridge-type with the jet pump cross-over connection and refluxes in the import and export two ends of mechanical pump, constitute a kind of reactor that has highly effective reaction function and conveying function with pump as the key reaction apparatus time, reaches the maximization that has caused effect.This reactor as the key reaction apparatus, not only exists violent turbulent flow and friction with pump in the system, also have frequently increasing suddenly and die-offing of pressure, and it is higher therefore to be applied under the response situation of gas-liquid two-phase efficient.The present invention only is made up of pump and pipeline, easy enforcement simple in structure.After determining, concrete reaction target can further optimize the supporting current return circuit of the mechanical pump of choosing variety classes, specification, material and different tube diameters, length.When the raw material quality of participating in reaction is very stable, can reach by each caliber place of valve of optimization system and cause the control effect, then omit some valves and even whole valves, further improve reactor and make economy.The present invention is considered as the pump of conveying machinery with tradition, is used as a kind of reactor, outside the intrinsic conveyer function of performance pump, fully excavates the potential reactor function of pump, and a kind of reactor of new high efficiency is provided.
Description of drawings
The present invention is further illustrated below in conjunction with accompanying drawing, wherein:
Fig. 1 is the schematic flow sheet of the present invention's first preferred embodiment;
Fig. 2 is the schematic flow sheet of the present invention's second preferred embodiment.
The specific embodiment
Fig. 1 is the schematic flow sheet of the present invention's first preferred embodiment, described bridge type pump reactor, and it comprises that 1, two jet pump 3 of a mechanical pump forms bridge-type by pipeline series connection cross-over connection and refluxes in the import and export two ends of this mechanical pump 1.The port of export of mechanical pump is connected with discharging opening, and the negative pressure mouth of jet pump connects charging aperture.Also be provided with return valve 2 on the pipeline of mechanical pump outlet, described discharging opening is connected with discharging valve 6, and return valve 2 and discharging valve 6 are used for control and reflux and response intensity.The charging aperture of described jet pump 3 is connected with charging valve 4, is used to control charge proportion.Also be provided with on the pipeline of described mechanical pump 1 import and start valve 5, according to the kind of selected mechanical pump with or need not, not this path cancellation of time spent.
As shown in Figure 1, mechanical pump 1 provides the reactor original power, and reaction medium enters the bridge-type return flow line through return valve 2, flows back to mechanical pump 1 import through jet pump 3.Reaction raw materials is inhaled into system through charging valve 4 simultaneously, after the reagentia through jet pump 3 and mechanical pump 1, through 6 outputs of discharging valve.
Fig. 2 is the schematic flow sheet of the present invention's second preferred embodiment, and the agent structure of this embodiment and operation principle are similar to first embodiment, and different is quantity and the mounting structure that adopts jet pump.In the present embodiment, adopt a jet pump to connect with the one group of jet pump that is formed in parallel by two jet pumps, these jet pump cohort cross-over connections form bridge-type and reflux in the import and export two ends of described mechanical pump 1 then.
According to actual condition, one group of jet pump cross-over connection can adopt a jet pump, also can adopting parallel connection and/or series connection forms bridge-type in the import and export two ends of described mechanical pump 1 and refluxes.
The present invention has the reactor of highly effective reaction function and conveying function as the key reaction apparatus time with pump, reach the maximization that has caused effect.The present invention is considered as the pump of conveying machinery with tradition, is used as a kind of reactor, outside the intrinsic conveyer function of performance pump, fully excavates the potential reactor function of pump, and a kind of reactor of new high efficiency is provided.The present invention only is made up of pump and pipeline, easy enforcement simple in structure.
Claims (4)
1. bridge type pump reactor, it is characterized in that comprising: a mechanical pump (1), at least one jet pump (3) form bridge-type by the pipeline cross-over connection and reflux in the import and export two ends of this mechanical pump (1), the port of export of described mechanical pump (1) is connected with discharging opening, and the negative pressure mouth of described jet pump (3) connects charging aperture; The pipeline of described mechanical pump (1) outlet is provided with return valve (2), and described discharging opening is connected with discharging valve (6), and return valve (2) and discharging valve (6) are used for control and reflux and response intensity.
2. bridge type pump reactor as claimed in claim 1 is characterized in that: described jet pump (3) is many, and it forms bridge-type by pipeline series connection and/or cross-over connection in parallel and refluxes in the import and export two ends of described mechanical pump (1).
3. bridge type pump reactor as claimed in claim 2 is characterized in that: the charging aperture of described jet pump (3) is connected with charging valve (4).
4. bridge type pump reactor as claimed in claim 3 is characterized in that, also is provided with on the pipeline of described mechanical pump (1) import to start valve (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101418940A CN101357318B (en) | 2008-09-09 | 2008-09-09 | Bridge type pump reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101418940A CN101357318B (en) | 2008-09-09 | 2008-09-09 | Bridge type pump reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101357318A CN101357318A (en) | 2009-02-04 |
| CN101357318B true CN101357318B (en) | 2011-05-11 |
Family
ID=40330002
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008101418940A Active CN101357318B (en) | 2008-09-09 | 2008-09-09 | Bridge type pump reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101357318B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107697971A (en) * | 2017-09-30 | 2018-02-16 | 北京海绵城市建设工程有限公司 | One kind is without air saturator type efficient air-floating apparatus |
-
2008
- 2008-09-09 CN CN2008101418940A patent/CN101357318B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN101357318A (en) | 2009-02-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101357318B (en) | Bridge type pump reactor | |
| CN100504267C (en) | System for recycling condensed water under high temperature | |
| CN102003419A (en) | Steam ejector composite set | |
| CN201225513Y (en) | High temperature viscous liquid conveyer | |
| CN203392243U (en) | Air-cannon material backflow prevention device | |
| GB2464881A (en) | Feed hopper for positive displacement pumps | |
| CN201502498U (en) | Unit pump of jet pump and vane type pump | |
| CN204234059U (en) | Pressure balance type reactor assembly | |
| CN106764222A (en) | Shell and tube fluid flow straightener | |
| CN102935945A (en) | Single efficient continuous delivery pump | |
| CN209100023U (en) | Shale gas pressure break mixing system | |
| CN202137943U (en) | Heating device of extruding system | |
| CN105697357A (en) | Inlet and outlet connecting structure of pump body | |
| CN214170752U (en) | Multi-pump parallel device | |
| CN202265116U (en) | Novel air cannon | |
| CN210029245U (en) | Pneumatic conveying pipeline gas distribution system | |
| CN211040932U (en) | Multifunctional boiler water supply deoxidization system | |
| CN202468187U (en) | Positive displacement diaphragm pump drainage self-priming pump | |
| CN201865991U (en) | Combined device for steam ejector | |
| CN105715349B (en) | Denoising device | |
| CN210164498U (en) | Gas extraction system | |
| CN102606533A (en) | Three-diffusion-tube volute structure enabling centrifugal pump to achieve radial force balance | |
| CN211275289U (en) | Coating and feeding device for efficient vacuum defoaming | |
| CN220082839U (en) | Sludge conveying pipeline | |
| CN201306257Y (en) | Novel cam pump apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |