CN202921172U - Membrane separation equipment - Google Patents
Membrane separation equipment Download PDFInfo
- Publication number
- CN202921172U CN202921172U CN 201220611576 CN201220611576U CN202921172U CN 202921172 U CN202921172 U CN 202921172U CN 201220611576 CN201220611576 CN 201220611576 CN 201220611576 U CN201220611576 U CN 201220611576U CN 202921172 U CN202921172 U CN 202921172U
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- membrane
- pilot plant
- heat exchanger
- plant test
- material pot
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model belongs to the technical field of separation equipment and particularly relates to membrane separation equipment. The bottom of a material pot is connected with a pressurizing pump; the pressurizing pump is connected with a heat exchanger; the heat exchanger is connected with a pilot plant test membrane assembly; the pilot plant test membrane assembly is connected with the upper part of the material pot; a membrane feeding pressure meter is arranged between the heat exchanger and the pilot plant test membrane assembly; and a membrane discharging pressure meter is arranged between the pilot plant test membrane assembly and the material pot. According to the membrane separation equipment disclosed by the utility model, all core parts of the membrane separation pilot plant test equipment are integrated and optimized to form normalized complete equipment so that the separation commonality is high, the volume is small, the weight is light, the structure is compact and the protection is complete; the automatic degree is high and the membrane separation equipment is convenient to use; and the reliability of a membrane separation pilot plant test experiment and the accuracy of detected data are greatly improved.
Description
Technical field
The utility model belongs to the separation equipment technical field, specifically a kind of membrane separation plant.
Background technology
Membrane separation technique refers at the mixture of different-grain diameter molecule on molecular level by pellicle the time, realize the technology of Selective Separation, pellicle claims again diffusion barrier or filter membrane, membranous wall is covered with aperture, can be divided into according to pore size: microfiltration membranes (MF), milipore filter (UF), NF membrane (NF), reverse osmosis membrane (RO) etc.It is to occur in 20 beginnings of the century that film separates, a separation technology that emerges rapidly after the sixties in 20th century.Membrane separation technique is owing to having separation, concentrated, purifying and refining function concurrently, efficient, energy-saving and environmental protection are arranged again, molecular level filters and filter process is simple, be easy to the feature such as control, therefore, food, medicine, biology, environmental protection, chemical industry, metallurgy, the energy, oil, water treatment, electronics, the field such as bionical have been widely used at present, produce huge economic benefit and social benefit, become one of most important means in current separation science.The membrane separation process parameter generally need to obtain through experiment, and existing film separates pilot plant, and versatility is poor, complex structure, and sample size is large, has inferior separating effect, and equipment is installed lack of standardization, etc. problem, thereby makes the accuracy that affects data.
Therefore, it is a can versatility good, simple in structure to design for above-mentioned situation, and sample size is little, good separating effect, a kind of membrane separation plant of equipment installation specification, inventor's problem that will solve just.
Summary of the invention
For the deficiencies in the prior art; defective and deficiency that the utility model exists in order to solve above-mentioned prior art; provide that a kind of volume is little, lightweight, compact conformation, protection be perfect, general a kind of membrane separation plant that automaticity is high has extraordinary practical value.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of membrane separation plant, comprise pilot scale membrane module, booster pump, material pot, heat exchanger, it is characterized in that: be connected with booster pump bottom material pot, booster pump is connected with heat exchanger, heat exchanger is connected with the pilot scale membrane module, the pilot scale membrane module is connected with material pot top, is provided with into the film pressure table between heat exchanger and pilot scale membrane module, is provided with the membrane Pressure gauge between pilot scale membrane module and material pot.
The beneficial effects of the utility model are:
1, the utility model separates each core component of pilot plant with film; normalized complete set of equipments after integration optimization in addition; make that it separates that versatility is high, volume is little, lightweight, compact conformation, protection be perfect; high being convenient to of automaticity moved, and greatly improved film and separated the reliability of pilot experiment and the accuracy of detection data.
Description of drawings
Fig. 1 is the utility model structural framing schematic diagram.
Description of reference numerals: 1-material pot; The 2-booster pump; The 3-heat exchanger; 4-advances the film pressure table; 5-pilot scale membrane module; 6-membrane Pressure gauge.
The specific embodiment
Below in conjunction with specific embodiment, further set forth the utility model, should be understood that these embodiment only are used for explanation the utility model and are not used in restriction scope of the present utility model.Should be understood that in addition those skilled in the art can make various changes or modifications the utility model after the content of having read the utility model instruction, these equivalent form of values drop on application appended claims limited range equally.
Fig. 1 is a kind of membrane separation plant structural framing of the utility model schematic diagram, comprise pilot scale membrane module 5, booster pump 2, material pot 1, heat exchanger 3, material pot 1 bottom is connected with booster pump 2, booster pump 2 is connected with heat exchanger 3, heat exchanger 3 is connected with pilot scale membrane module 5, pilot scale membrane module 5 is connected with material pot 1 top, be provided with into film pressure table 4 between heat exchanger 3 and pilot scale membrane module 5, be provided with membrane Pressure gauge 6 between pilot scale membrane module 5 and material pot 1, the utility model separates each core component of pilot plant with film, normalized complete set of equipments after integration optimization in addition, make its separation versatility high, volume is little, lightweight, compact conformation, protect perfect, high being convenient to of automaticity moved, greatly improve film and separated the reliability of pilot experiment and the accuracy of detection data.
Claims (1)
1. membrane separation plant, comprise pilot scale membrane module, booster pump, material pot, heat exchanger, it is characterized in that: be connected with booster pump bottom material pot, booster pump is connected with heat exchanger, heat exchanger is connected with the pilot scale membrane module, the pilot scale membrane module is connected with material pot top, is provided with into the film pressure table between heat exchanger and pilot scale membrane module, is provided with the membrane Pressure gauge between pilot scale membrane module and material pot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220611576 CN202921172U (en) | 2012-11-19 | 2012-11-19 | Membrane separation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220611576 CN202921172U (en) | 2012-11-19 | 2012-11-19 | Membrane separation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202921172U true CN202921172U (en) | 2013-05-08 |
Family
ID=48211166
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220611576 Expired - Fee Related CN202921172U (en) | 2012-11-19 | 2012-11-19 | Membrane separation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202921172U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107469623A (en) * | 2017-09-25 | 2017-12-15 | 厦门市天泉鑫膜科技股份有限公司 | A kind of multifunctional membrane separates pilot experiment equipment |
-
2012
- 2012-11-19 CN CN 201220611576 patent/CN202921172U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107469623A (en) * | 2017-09-25 | 2017-12-15 | 厦门市天泉鑫膜科技股份有限公司 | A kind of multifunctional membrane separates pilot experiment equipment |
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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: 20130508 Termination date: 20151119 |
|
| EXPY | Termination of patent right or utility model |