CN202609583U - Compressed variable pressure powder pump device - Google Patents
Compressed variable pressure powder pump device Download PDFInfo
- Publication number
- CN202609583U CN202609583U CN 201220252138 CN201220252138U CN202609583U CN 202609583 U CN202609583 U CN 202609583U CN 201220252138 CN201220252138 CN 201220252138 CN 201220252138 U CN201220252138 U CN 201220252138U CN 202609583 U CN202609583 U CN 202609583U
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- pump body
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- powder
- feed pipe
- pump housing
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- Expired - Lifetime
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- 239000000843 powder Substances 0.000 title claims abstract description 53
- 230000006835 compression Effects 0.000 claims abstract description 5
- 238000007906 compression Methods 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 abstract description 22
- 230000009466 transformation Effects 0.000 description 20
- 238000000034 method Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 9
- 238000005086 pumping Methods 0.000 description 9
- 230000033001 locomotion Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
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Abstract
本实用新型公开了一种压缩型变压粉体泵装置，包括进料管、泵体直筒段和泵体锥筒段，所述泵体直筒段与水平方向呈一定的夹角，在泵体直筒段内沿轴心设置活塞杆，所述活塞杆的端部设有与泵体直筒段内孔相适配的活塞；在泵体直筒段的上半段设置入口阀门，在泵体直筒段的下半段设置过滤器；所述进料管的上端与常压料仓的出料口连通，进料管的下端与入口阀门连通；所述泵体锥筒段的大口端与泵体直筒段的下端连通，在泵体锥筒段的小口端设置粉体出口。本实用新型可替代仓泵输送系统中的变压仓，有效避免因料仓中架桥等问题而导致的整个粉体输送系统的工作不稳定，提高输送系统的可靠性，实现了对高压输送仓的连续加料，保持高压输送仓内料位基本不变，使粉体的流化状态稳定，输料稳定连续。
The utility model discloses a compression type variable pressure powder pump device, which comprises a feed pipe, a pump body straight barrel section and a pump body cone barrel section, the pump body straight barrel section and the horizontal direction form a certain angle, A piston rod is arranged along the axis in the straight barrel section, and a piston matching the inner hole of the straight barrel section of the pump body is arranged at the end of the piston rod; an inlet valve is set on the upper half of the straight barrel section of the pump body, and A filter is set in the half section; the upper end of the feed pipe is connected with the discharge port of the atmospheric pressure silo, and the lower end of the feed pipe is connected with the inlet valve; the large mouth end of the pump body cone section is connected with the pump body straight section. The lower end is connected, and the powder outlet is set at the small mouth end of the cone section of the pump body. The utility model can replace the variable pressure chamber in the warehouse pump conveying system, effectively avoid the unstable operation of the entire powder conveying system caused by problems such as bridging in the chamber, improve the reliability of the conveying system, and realize high-pressure conveying The continuous feeding of the bin keeps the material level in the high-pressure conveying bin basically unchanged, so that the fluidized state of the powder is stable and the feeding is stable and continuous.
Description
Technical field
The utility model relates to a kind of compression-type transformation powder pumping plant, is applicable to the powder conveying in the industrial process such as extensive dry powder gasification, IGCC generating, chemical industry, metallurgy, pharmacy and food processing.
Background technology
The high pressure Dense Phase Pneumatic Conveying is widely used in extensive dry coal powder gasification and chemical field, and the processing of powder material and carry to adopt lock bucket system to carry out transformation comprises the transformation conveying, slagging-off of powder material etc.
In the transformation delivery system of powder; Powder normal pressure storehouse is a low-pressure system; The conveying feed bin is a high-pressure system; The transformation storehouse is high pressure, low pressure alternate system, and powder is uprised pressure, accomplished the process realization that continuous-feeding is the such repeat of pressurization-blowing-pressure release-charging-pressurization through the transformation storehouse by low pressure.In this system, because the operation of transformation storehouse is the process of a pressure alternation, operating conditions is more abominable, and failure frequency is higher, and the lock bucket is easy to generate phenomenons such as knot arch, bridge formation, false material level in the blanking process, cause the blanking process not smooth.Because lock bucket cycle blowing causes high-pressure delivery bin-level periodically-varied, and then causes the fugitiveness of fluidisation or the complexity of controlling, the fugitiveness and the discountinuity that cause coal dust to be carried.
Summary of the invention
Goal of the invention: the utility model to transformation warehousing in the prior art defective or deficiency, a kind of compression-type transformation powder pumping plant that can substitute the transformation storehouse is provided.
In order to solve the problems of the technologies described above, the utility model has adopted following technical scheme:
A kind of compression-type transformation powder pumping plant; Comprise feed pipe, pump housing direct tube section and pump housing conical cylinder section; Said pump housing direct tube section and horizontal direction are certain included angle, in pump housing direct tube section, along the axle center piston rod are set, and the end of said piston rod is provided with and the suitable piston of pump housing direct tube section endoporus; At the upper semisection inlet porting valve of pump housing direct tube section, at the lower semisection of the pump housing direct tube section filter is set, pump housing direct tube section inner through filter with cushion air chamber and be communicated with; The upper end of said feed pipe is communicated with the discharging opening of normal pressure feed bin, and the lower end of feed pipe is communicated with inlet valve, at the middle part of feed pipe the charging valve is set; The big opening end of said pump housing conical cylinder section is communicated with the lower end of pump housing direct tube section, at the osculum end of the pump housing conical cylinder section powder outlet is set, and on the pump housing conical cylinder section near the powder outlet, outlet valve is set.
In the utility model, further, the inwall of said pump housing direct tube section is a smooth inner wall, and the inwall of pump housing conical cylinder section is rough inwall.
Compared with prior art, the utlity model has following advantage:
(1) the transformation storehouse in the pump delivery system of alternative storehouse, the job insecurity of the whole powder delivery system of effectively avoiding causing because of problem such as build bridge in the feed bin improves the reliability of delivery system;
(2) change the alternately abominable service conditions of transformation, avoid the use of involve great expense, lock bucket valve that limited service life, fault take place frequently, effectively reduce high-pressure air source consumption;
(3) realization is to the continuous charging in high-pressure delivery storehouse, and material level is constant basically in the high conveying of the maintenance storehouse, makes the fluidized state of powder stable, fails and expects steady and continuous;
(4) simple and compact for structure, easy for installation, volume is little, and is in light weight, and mounting arrangements does not receive the layout in factory building space, and construction costs is low;
(5) can accomplish transformation, the course of conveying that carries out powder material.
Description of drawings
Fig. 1 is the powder delivery system scheme drawing that has the compression-type transformation powder pumping plant of the utility model.
Fig. 2 is the structural representation of the utility model.
The specific embodiment:
Below in conjunction with accompanying drawing the utility model is done explanation further.
As shown in Figure 1, powder adds powder delivery system from the top of normal pressure feed bin 13, under normal pressure, gets into the compression-type transformation powder pumping plant of the utility model, in compression-type transformation powder pumping plant, pressurizes, and delivers to high-pressure delivery storehouse 15 then.
As shown in Figure 2, the compression-type transformation powder pumping plant of the utility model comprises feed pipe 1, pump housing direct tube section 4 and pump housing conical cylinder section 10.Said pump housing direct tube section 4 is certain included angle with horizontal direction; Piston rod 6 is set along the axle center in pump housing direct tube section 4; The end of said piston rod 6 is provided with and the suitable piston 5 of pump housing direct tube section 4 endoporus, and the inwall of pump housing direct tube section 4 is a smooth inner wall, and piston 5 is good with pump housing direct tube section 4 inner wall sealings; Piston rod 6 is driven by high pressure cylinder, can be along the axis free motion of pump housing direct tube section 4.At the upper semisection inlet porting valve 3 of pump housing direct tube section 4, at the lower semisection of pump housing direct tube section 4 filter 7 is set, filter 7 adopts porous sintered metal materials to process, pump housing direct tube section 4 inner through filters 7 with cushion air chamber 8 and be communicated with.The upper end of said feed pipe 1 is communicated with the discharging opening of normal pressure feed bin 13 lower ends, and the lower end of feed pipe 1 is communicated with inlet valve 3, at the middle part of feed pipe 1 charging valve 2 is set.Inlet valve 3 is by the periodic opening and closing of programming control, and piston 5 is opened inlet valve 3 after inlet valve 3 positions are crossed in bottom dead point B motion, and piston 5 is closed inlet valve 3 when no show inlet valve 3 positions are gone back in top dead point A motion.The big opening end of said pump housing conical cylinder section 10 is communicated with the lower end of pump housing direct tube section 4, at the osculum end of pump housing conical cylinder section 10 powder outlet 12 is set, and on the pump housing conical cylinder section 10 near powder outlet 12, outlet valve 11 is set.The inwall of pump housing conical cylinder section 10 is rough inwall (having certain roughness), prevents that powder material is moved under differential pressure action for 9 layers.
At first close outlet valve 11 when the compression-type transformation powder pumping plant of the utility model is worked, open charging valve 2, inlet valve 3, a certain amount of powder material 9 is entering pump housing direct tube section 4 under the run by gravity effect, closes inlet valve 3; Piston 4 is moved to top dead point A by bottom dead point B; Promoting powder material 9 moves to pump housing conical cylinder section 10; Delivering gas in pump housing direct tube section 4 and the pump housing conical cylinder section 10 process filters 7 under the effect of volume compression get in the buffering air chambers 8 simultaneously, and 9 processes of powder material are filtered and stayed in pump housing direct tube section 4 and the pump housing conical cylinder section 10; Return behind the piston arrives top dead point A; Cavity volume between piston 5 and the outlet valve 11 increases; Gaseous tension reduces, the delivering gas cubic expansion in the buffering air chamber 8, and portion gas is back to again in the pump housing direct tube section 4; When piston 5 was got back to bottom dead point B, gaseous tension returned to normal pressure in the cavity of pump housing direct tube section 4 and pump housing conical cylinder section 10; Open inlet valve 3 this moment once more, and a certain amount of powder material 9 can fall into pump housing direct tube section 4 smoothly; Behind the several said process, be full of powder material 9 in the top dead point A of piston 5 motions and the cavity between the outlet valve 11, and powder material 9 is compressed to certain intensity; Open outlet valve 11; The powder material 9 of compression this moment is combined closely with pump housing tapering 10 coarse walls; Prevent that powder material is moved under differential pressure action for 9 layers, powder material 9 intergranular gaps are very little, and the gas in high-pressure delivery storehouse 15 is difficult to penetrate powder material 9 and gets into pump housing direct tube section 4; Open inlet valve 2 once more, a certain amount of powder material 9 gets into pump housing direct tube section 4 inside that are in atmospheric pressure state under the run by gravity effect, close inlet valve 2; Piston 5 promotes powder material 9 and moves to pump housing conical cylinder section 10; Under the powerful impetus of piston; The powder material 9 of this batch entering pump housing direct tube section 4 contacts with preceding batch powder material 9 and tight compression, and the powder material in the pump housing conical cylinder section 10 9 is clamp-oned high-pressure delivery storehouse 15 through powder outlet 12.Repeat above-mentioned cyclic process, just can realize continuous charging the high-pressure delivery storehouse.
The above only is the preferred implementation of the utility model; Should be pointed out that for those skilled in the art, under the prerequisite that does not break away from the utility model principle; Can also make some improvement and retouching, these improvement and retouching also should be regarded as the protection domain of the utility model.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220252138 CN202609583U (en) | 2012-05-31 | 2012-05-31 | Compressed variable pressure powder pump device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220252138 CN202609583U (en) | 2012-05-31 | 2012-05-31 | Compressed variable pressure powder pump device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202609583U true CN202609583U (en) | 2012-12-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220252138 Expired - Lifetime CN202609583U (en) | 2012-05-31 | 2012-05-31 | Compressed variable pressure powder pump device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202609583U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102700940A (en) * | 2012-05-31 | 2012-10-03 | 东南大学 | Compression type variable-pressure powder pump device |
| CN103922146A (en) * | 2014-05-08 | 2014-07-16 | 上海边锋泵业制造有限公司 | Particle pump |
| CN105151793A (en) * | 2015-08-21 | 2015-12-16 | 天津宜诺医药工业设计有限公司 | Powder conveying pipe and conveying method thereof |
| CN106144608A (en) * | 2016-08-22 | 2016-11-23 | 李福军 | Powder stablizes controlled delivery device and method |
| CN113086648A (en) * | 2021-04-12 | 2021-07-09 | 浙江中创科联智能装备技术有限公司 | Conveying and metering device for powder auxiliaries for printing and dyeing industry |
-
2012
- 2012-05-31 CN CN 201220252138 patent/CN202609583U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102700940A (en) * | 2012-05-31 | 2012-10-03 | 东南大学 | Compression type variable-pressure powder pump device |
| CN103922146A (en) * | 2014-05-08 | 2014-07-16 | 上海边锋泵业制造有限公司 | Particle pump |
| CN105151793A (en) * | 2015-08-21 | 2015-12-16 | 天津宜诺医药工业设计有限公司 | Powder conveying pipe and conveying method thereof |
| CN106144608A (en) * | 2016-08-22 | 2016-11-23 | 李福军 | Powder stablizes controlled delivery device and method |
| CN113086648A (en) * | 2021-04-12 | 2021-07-09 | 浙江中创科联智能装备技术有限公司 | Conveying and metering device for powder auxiliaries for printing and dyeing industry |
| CN113086648B (en) * | 2021-04-12 | 2022-07-12 | 浙江中创科联智能装备技术有限公司 | Conveying and metering device for powder auxiliaries for printing and dyeing industry |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20121219 Effective date of abandoning: 20140507 |
|
| RGAV | Abandon patent right to avoid regrant |