CN104819118A - Pump improved structure and manufacturing method thereof - Google Patents

Pump improved structure and manufacturing method thereof Download PDF

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Publication number
CN104819118A
CN104819118A CN201410841012.7A CN201410841012A CN104819118A CN 104819118 A CN104819118 A CN 104819118A CN 201410841012 A CN201410841012 A CN 201410841012A CN 104819118 A CN104819118 A CN 104819118A
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China
Prior art keywords
ceramic layer
pump
layer
modified node
frp
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CN201410841012.7A
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CN104819118B (en
Inventor
罗国兵
蓝伟光
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Suntar Membrane Technology Xiamen Co Ltd
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Suntar Membrane Technology Xiamen Co Ltd
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Publication of CN104819118A publication Critical patent/CN104819118A/en
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Abstract

The invention discloses a pump improved structure and a manufacturing method thereof; liquid conveying parts all adopt double-layer structures; the pump improved structure comprises a ceramic layer at the inner side, and a glass steel layer at the outer side, wherein the glass steel layer is 5-20 mm thick; the ceramic layer is an aluminum oxide ceramic layer; in the ceramic layer, the content of Al2O3 is higher than 99%; after the constant-temperature pressure keeping sintering is performed for 8-10 h at a highest temperature of 1850-1950 DEG C in sintering, the cooling and the discharge from a furnace are performed; then, the constant-pressure permeation is performed for the ceramic layer in a high pressure-resistant pressure container by unsaturated polyester resins under the pressure of 25-38 MPa for at least 4 h; and finally, the ceramic layer is stably cured in a constant-temperature drying tank. The pump improved structure resists corrosion and has high pressure performance.

Description

A kind of pump modified node method and manufacture method thereof
Technical field
The present invention relates to a kind of pump modified node method and manufacture method thereof.
Background technique
Along with industrial expansion, the pressure of environmental protection is also increasing.The process of some industrial acid-bearing wastewaters, desalination of sea water, soda acid recovery etc. all extensively needs to use various pump to carry liquid.
Traditional high-pressure service pump pressure can reach 4Mpa, and some inlet pump pressure may reach higher.But have following shortcomings, even if pressure gets on, still flow does not increase, and is substantially all high-lift low discharge on the market.In addition, existing high-pressure service pump all becomes substantially in not corrosion resistant shortcoming.And for traditional anti-corrosive pump, than example hydrochloric acid pump, often all in a few MPa at zero point, be difficult to the requirement meeting high pressure far away.Therefore, existing pump has similar contradiction, can not meet the requirement of high pressure and corrosion-resistant two aspects simultaneously.
Summary of the invention
The object of the present invention is to provide a kind of manufacture method of pump modified node method, to solve the above-mentioned problems in the prior art.
Technological scheme provided by the invention is as follows:
A manufacture method for pump modified node method, wherein, on the position (with the position that liquid directly contacts) of high-pressure service pump conveying liquid, all adopt double layer construction, comprise the ceramic layer being positioned at inner side and the frp layer being positioned at outside, wherein, the thickness of frp layer is 5-20mm; Ceramic layer is alumina ceramic layer, and in this ceramic layer, the content of Al2O3 is greater than 99%, and when sintering, after maximum temperature sinters 8h-10h under constant temperature pressurize at 1850 DEG C-1950 DEG C, cooling down is come out of the stove; Afterwards, ceramic layer in high voltage bearing pressurized container, use 25Mpa-38Mpa pressure under, use unsaturated polyester resin, through at least 4 hours constant voltages infiltration, finally in thermostatic drying chamber through stable curing.
Wherein, the position of conveying liquid of the present invention comprises pump core, runner, spool.
In the preferred embodiment, described unsaturated polyester resin is U.S. Ya Shilan food-grade K530.
In the preferred embodiment, frp layer thickness is 8-12mm.Be preferably 10mm.
In the preferred embodiment, the thickness of ceramic layer is 5-100mm, is preferably 10-50mm.
In the preferred embodiment, thermostatic drying chamber temperature is 60-90 DEG C, and the time is 24h-120h.
In the preferred embodiment, constant voltage time of penetration is 4-100h.
Wherein, ceramic layer generates the method for FRP is outward traditional glass fibre reinforced plastics lamination process.
A kind of modified node method of pump, it is characterized in that: on the position of high-pressure service pump conveying liquid, all adopt double layer construction, comprise the ceramic layer being positioned at inner side and the frp layer being positioned at outside, wherein, ceramic layer thickness is 5-100mm, and frp layer thickness is 5-20mm, this ceramic layer, for using unsaturated polyester resin, forms through the constant voltage infiltrations of at least 4 hours and solidification.
Seen from the above description, the invention provides a kind of manufacture method of pump modified node method,
1, in the FRP material that the skin of ceramicpump core, spool, runner is lining with, pottery itself has very strong corrosion resistance, but enbrittle, the present invention acid resistant alkali resin with the mode of high-pressure osmosis penetrate into pottery hole in go, isothermal curing again, again at its external sheath one deck 5-20mm glass fibre reinforced plastics, find that it can overcome the shortcoming of the high pressure fragility of ceramic material effectively.
2, after ceramic post sintering, there is tiny hole ceramic inside, and in order to make its water tightness better, mechanical strength is higher.Acid resistant alkali resin penetrates in the hole of pottery in the mode of high-pressure osmosis and goes, and can solve the intrinsic hard defects of pottery like this.
Experiment proves that the pump of structure of the present invention can at the pressure of 3Mpa-5Mpa, and fluid is the hydrochloric acid of 25% concentration, and temperature is effectively run under the operating mode of 40 DEG C.Meet high pressure resistant and corrosion resistant requirement simultaneously.
Accompanying drawing explanation
Fig. 1 is the Facad structure schematic diagram of pump of the present invention;
Fig. 2 is the side structure schematic diagram of pump of the present invention;
Fig. 3 is partial schematic diagram.
In figure
1-motor 2-speed reducer 3-coupling 4-base 5-import 6-exports
7-pumping cylinder 8-inlet valve 9-outlet valve 10-flange 11-connecting body 12-oil hole
13-rear view window 14-axle cover 15-housing
Embodiment
Specific embodiments of the invention, see figures.1.and.2, a kind of modified node method of pump, are a high-pressure plunger pump, comprise a base 4, base are installed speed reducer 2, and the left side of speed reducer connects motor 1, and the right side of speed reducer 2 connects coupling 3.The right side of coupling 3 is the pump housing.The outside of this pump housing comprises housing 15, and axle cover 14 is established at the rear, right side of housing 15, and rear side establishes rear view window 13.Upper surface middle part establishes oil hole 12.
Wherein, the output shaft of motor (1) is connected with coupling (3), and coupling (3) connects speed reducer (2), and speed reducer (2) connects the pump housing by linking mechanism.This pump housing comprises a housing 15, and in the front side of housing 15, if three pumping cylinders 7 side by side, these three pumping cylinders 7 share an import 5 and share an outlet 6, and these three pumping cylinder 7 connecting bodys 11 connect.An outlet valve 9 is established in the top of each pumping cylinder 7, and an inlet valve 8 is established in below.
See Fig. 3, pumping cylinder 7 is made for materials at two layers, comprises the ceramic layer 7-1 being positioned at inner side and FRP (glass fibre reinforced plastics) the layer 7-2 being positioned at outside, wherein, the thickness of frp layer 7-2 is 10mm, as required, the thickness of ceramic layer 7-1 can be 5-100mm, is preferably 10-50mm.In addition, and the runner 16 of liquid comes into contact is also for materials at two layers is made, and comprise the ceramic layer 16-1 being positioned at inner side and the frp layer 16-2 being positioned at outside, wherein, the thickness of frp layer 16-2 is 10mm.As required, the thickness of ceramic layer 16-1 can be 5-100mm, is preferably 10-50mm.
Wherein, ceramic layer is alumina ceramic layer, in this ceramic layer, and Al 2o 3content be greater than 99%, sinter time, maximum temperature at 1850 DEG C-1950 DEG C after constant temperature pressurize 8h-10h cooling down come out of the stove.Afterwards, ceramic layer is in high voltage bearing pressurized container, under using the pressure of 25Mpa-38Mpa, use import U.S. Ya Shilan food-grade K530 unsaturated polyester resin, through 8 hours constant voltages infiltration make it have more reliable permeability, finally in the thermostatic drying chamber of 80 degree through 72 hours stable curings.
Finally, generate the glass fibre reinforced plastics of 10mm at ceramic layer outward, method is for adopting traditional-handwork lamination mould-forming process.Experiment proves that pump of the present invention can at the pressure of 3Mpa-5Mpa, and fluid is the hydrochloric acid of 25% concentration, and temperature is effectively run under the operating mode of 40 DEG C.
Above are only a specific embodiment of the present invention, but design concept of the present invention is not limited thereto, all changes utilizing this design the present invention to be carried out to unsubstantiality, all should belong to the behavior of invading scope.

Claims (8)

1. a manufacture method for pump modified node method, is characterized in that: on the position of high-pressure service pump conveying liquid, all adopts double layer construction, and comprise the ceramic layer being positioned at inner side and the frp layer being positioned at outside, wherein, the thickness of frp layer is 5-20mm; Ceramic layer is alumina ceramic layer, in this ceramic layer, and Al 2o 3content be greater than 99%, sinter time, maximum temperature at 1850 DEG C-1950 DEG C after constant temperature pressurize 8h-10h cooling down come out of the stove; Afterwards, ceramic layer in high voltage bearing pressurized container, use 25Mpa-38Mpa pressure under, use unsaturated polyester resin, through at least 4 hours constant voltages infiltration, finally in thermostatic drying chamber through stable curing; After solidification, then generate frp layer outward at ceramic layer.
2. the manufacture method of a kind of pump modified node method as claimed in claim 1, is characterized in that: the position of described conveying liquid comprises pump core, runner, spool.
3. the manufacture method of a kind of pump modified node method as claimed in claim 1, is characterized in that: described unsaturated polyester resin is U.S. Ya Shilan food-grade K530.
4. the manufacture method of a kind of pump modified node method as claimed in claim 1, is characterized in that: frp layer thickness is 8-12mm.
5. the manufacture method of a kind of pump modified node method as claimed in claim 1, is characterized in that: the thickness of ceramic layer is 5-100mm.
6. the manufacture method of a kind of pump modified node method as claimed in claim 1, it is characterized in that: thermostatic drying chamber temperature is 60-90 DEG C, the time is 24h-120h.
7. the manufacture method of a kind of pump modified node method as claimed in claim 1, is characterized in that: ceramic layer generates the method for FRP outward for adopting traditional-handwork lamination mould-forming process.
8. the modified node method of a pump, it is characterized in that: on the position of high-pressure service pump conveying liquid, all adopt double layer construction, comprise the ceramic layer being positioned at inner side and the frp layer being positioned at outside, wherein, ceramic layer thickness is 5-100mm, and frp layer thickness is 5-20mm, this ceramic layer, for using unsaturated polyester resin, forms through the constant voltage infiltrations of at least 4 hours and solidification.
CN201410841012.7A 2014-12-30 2014-12-30 A kind of pump improved structure and its manufacture method Active CN104819118B (en)

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CN104819118B CN104819118B (en) 2017-03-08

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040202548A1 (en) * 2003-04-09 2004-10-14 Xunhu Dai Micropump with integrated pressure sensor
CN103591049A (en) * 2013-10-18 2014-02-19 宜兴市宙斯泵业有限公司 Cracking-preventive wear-resistant centrifugal pump
CN103807163A (en) * 2014-01-22 2014-05-21 合肥精创陶瓷设备科技有限公司 Split type slurry pump cylinder sleeve
CN203718172U (en) * 2014-01-17 2014-07-16 万俊松 Novel concrete pump truck conveying pipeline

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040202548A1 (en) * 2003-04-09 2004-10-14 Xunhu Dai Micropump with integrated pressure sensor
CN103591049A (en) * 2013-10-18 2014-02-19 宜兴市宙斯泵业有限公司 Cracking-preventive wear-resistant centrifugal pump
CN203718172U (en) * 2014-01-17 2014-07-16 万俊松 Novel concrete pump truck conveying pipeline
CN103807163A (en) * 2014-01-22 2014-05-21 合肥精创陶瓷设备科技有限公司 Split type slurry pump cylinder sleeve

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