CN104806484A - Carbon monoxide compressor filtering system capable of overhauling and replacing filter online - Google Patents
Carbon monoxide compressor filtering system capable of overhauling and replacing filter online Download PDFInfo
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- CN104806484A CN104806484A CN201410040429.3A CN201410040429A CN104806484A CN 104806484 A CN104806484 A CN 104806484A CN 201410040429 A CN201410040429 A CN 201410040429A CN 104806484 A CN104806484 A CN 104806484A
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- filter
- carbon monoxide
- stop valve
- front filter
- bypass line
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Abstract
The invention relates to a carbon monoxide compressor filtering system capable of overhauling and replacing a filter online. The system is that a compressed air pipeline is connected to an outlet of a carbon monoxide compressor; a front filter is arranged on the compressed air pipeline; a filter bypass pipeline, a rear filter and a rear filter bypass pipeline are arranged on the compressed air pipeline; the rear filter and the rear filter bypass pipe are arranged at the downstream of the front filter; stop valves are arranged at two ends of an inlet and an outlet of the front filter; the stop valves are arranged at two ends of the inlet and the outlet of the rear filter; the stop valves are arranged on the front filter bypass pipeline and the rear filter bypass pipeline. Compared with the prior art, the system has the advantages that two filters are arranged, and one filter can be replaced or overhauled while another filter is used, so that the work cannot be stopped; the system has the advantages of being wide in applicable scope, safe and reliable.
Description
Technical field
The present invention relates to a kind of compressor filtration system, especially relate to and a kind ofly can change the carbon monoxide compressor filtration system of filter by on-bne repair.
Background technique
At present, carbon monoxide compressor mainly in order to carbon monoxide pressurization designed by compressor, in order to the purity of the high pressure carbon monoxide product of carbon monoxide after compressor pressurizes, usually can increase a carbon monoxide filter.But carbon monoxide is by compressor process, cylinder and pressurized gas can be there are there is friction thus produce carbon dust, this will make pressure reduction before and after carbon monoxide filter gradually raise, thus the filter core in carbon monoxide filter is blocked, carbon monoxide product cannot be normal through, causes stopping supplying client.At this time just need to stop carbon monoxide compressor to change the filter core in carbon monoxide filter.
Related documents also discloses many switch filtering devices in parallel has good guarantee for the stable persistency in production process, but be mainly still applied to if water, ammonia, oil product, hydro carbons are main, because the possibility of its impurity existed of this kind of article is present in fluid and gas itself.And the machine body cylinder of carbon monoxide compressor and CO (carbon monoxide converter) gas rub, the filtration of the large particle carbon dust produced is not suitable for structure recited above.
Summary of the invention
Object of the present invention is exactly to overcome the defect and provide a kind of using scope wide, safe and reliable can change the carbon monoxide compressor filtration system of filter by on-bne repair that above-mentioned prior art exists.
Object of the present invention can be achieved through the following technical solutions:
A kind ofly can change the carbon monoxide compressor filtration system of filter by on-bne repair, the outlet of carbon monoxide compressor connects pressurized gas pipeline, this pressurized gas pipeline is provided with front filter, described pressurized gas pipeline is also provided with front filter bypass line, after-filter and after-filter bypass line, described after-filter and after-filter bypass line are located at the downstream of front filter, the import and export two ends of described front filter are provided with stop valve, and the import and export two ends of described after-filter are provided with stop valve; Described front filter bypass line and after-filter bypass line are equipped with stop valve.
The import and export of described front filter bypass line are positioned at the outside of the stop valve at the import and export two ends of front filter;
The import and export of described after-filter bypass line are positioned at the outside of the stop valve at the import and export two ends of after-filter.
The both sides that front filter imports and exports the stop valve at two ends are all provided with blind plate; The both sides that the stop valve at two ends imported and exported by after-filter are all provided with blind plate.
Described front filter and the top of after-filter are equipped with pressure relief valve.
Described front filter and after-filter all adopt model to be the filter of bohr MCC1401E500H13, and design pressure is 2.0MPA, design temperature is 80 DEG C, weight is 440KG.
Described front filter is identical with the internal structure of after-filter, primarily of suction flange head, outlet(discharge) flange head, filter body, filter core, blind flange, leads pouring and fastening piece composition.
Carbon monoxide is 1.6MPA in the ducted operational condition of pressurized gas, 40 DEG C, and the design condition of pressurized gas pipeline is 1.85MPA, 40 DEG C.
Working principle of the present invention is:
In the present invention, after-filter is connected on front filter downstream, first front filter is used during use, stop valve now on front filter bypass line is closed, the stop valve that two ends imported and exported by after-filter is closed, compression carbon monoxide is after front filter, then through this flow process of after-filter bypass line, original production status can normally be kept.
When front filter pressure reduction is higher than 0.75bar, illustrate that the filter core of front filter has blocking, when needing to keep in repair front filter, the stop valve directly front filter can being imported and exported two ends is closed, and opens the stop valve on front filter bypass line, opens the stop valve that two ends imported and exported by after-filter, and the stop valve of closing on after-filter bypass line, front filter can be unloaded like this and carry out more renew cartridge or maintenance, play remaining normal and produce, again the object of more renew cartridge.
After front filter maintenance process, normal mode can be switched to, both front filter was arranged on pressurized gas pipeline, and opened the stop valve that front filter imports and exports two ends, the stop valve on front filter bypass line is closed, the stop valve that two ends imported and exported by after-filter is opened, close the stop valve on after-filter bypass line, compression carbon monoxide through front filter, by the pattern of filter later, to prevent after-filter after pressure reduction raises, directly affect product pressure.
Compared with prior art, the present invention has the following advantages and beneficial effect:
One, using scope is wide: because similar carbon monoxide compressor can exist the problem of cylinder similar equally and gas friction generation carbon dust, so system of the present invention can be applied to the compressor of same medium.
Two, safe and reliable: because newly-increased after-filter is that be through gas pressure testing for pressure-bearing aspect, two filters can bear the too high danger of gas pressure according to front filter design.In addition for system decompression, because pressure relief valve is all equipped with in the top of front filter and after-filter, by the direct pressure release of top hand valve.
Three, long-term benefit: due to this carbon monoxide compressor directly faced by be Product supply client, therefore stop supplying to be exactly direct economic loss for enterprise, and system of the present invention can repair or replace filter core to filter by direct-on-line, the normal operation of production can not be affected.
Four, maintenance is convenient: there is blind plate the stop valve both sides importing and exporting two ends due to front filter or after-filter, can excise filter fast, and with blind plate isolation, there is not the problem of keeping in repair and leaking early stage.
Accompanying drawing explanation
Fig. 1 is existing carbon monoxide compressor filtration system structural representation:
Fig. 2 is carbon monoxide compressor filtration system structural representation of the present invention;
Fig. 3 is the structural representation of front filter.
In figure, 1 is carbon monoxide compressor, and 2 is pressurized gas pipeline, 3 is front filter, and 4 is front filter bypass line, and 5 is after-filter, 6 is after-filter bypass line, and 7 is stop valve, and 8 is pressure relief valve, 31 is top end socket, and 32 is suction flange, and 33 is inlet pressure sensing point, 34 is inlet guide pouring, and 35 is outlet(discharge) flange, and 36 is that outlet guide drenches, 37 is outlet pressure sensing point, and 38 is filter core, and 39 is top blow-down pipe.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is described in detail.
Comparative example
Existing carbon monoxide compressor filtration system as shown in Figure 1, the outlet of carbon monoxide compressor 1 connects pressurized gas pipeline 2, this pressurized gas pipeline 2 is provided with front filter 3, pressurized gas pipeline 2 is also provided with front filter bypass line 4, the import and export two ends of front filter 3 are provided with stop valve 7, compress carbon monoxide during use and enter into equipment needed thereby after front filter 3, when needs are changed or keep in repair front filter 3, could keep in repair after needing the stop valve 7 front filter 3 being imported and exported two ends to close, can not repair and replacement online, stop for carbon monoxide is exactly direct economic loss for enterprise.
Embodiment
A kind of carbon monoxide compressor filtration system can depositing line examine and replace filter, as shown in Figure 2, the outlet of carbon monoxide compressor 1 connects pressurized gas pipeline 2, this pressurized gas pipeline 2 is provided with front filter 3, pressurized gas pipeline 2 is also provided with front filter bypass line 4, after-filter 5 and after-filter bypass line 6, the import and export two ends of front filter 3 are provided with stop valve 7, after-filter 5 and after-filter bypass line 6 are located at the downstream of front filter 3, and the import and export two ends of after-filter 5 are provided with stop valve 7; Front filter bypass line 4 and after-filter bypass line 6 are equipped with stop valve 7.The import and export of front filter bypass line 4 are positioned at the outside of the stop valve 7 at the import and export two ends of front filter 3; The import and export of after-filter bypass line 6 are positioned at the outside of the stop valve 7 at the import and export two ends of after-filter 5.The both sides that front filter 3 imports and exports the stop valve 7 at two ends are all provided with blind plate; The both sides that the stop valve 7 at two ends imported and exported by after-filter 5 are all provided with blind plate.Front filter 3 is equipped with pressure relief valve 8 with the top of after-filter 5.
Front filter 3 and after-filter 5 all adopt model to be the filter of bohr MCC1401E500H13, and design pressure is 2.0MPA, design temperature is 80 DEG C, weight is 440KG.
Front filter 3 is identical with the internal structure of after-filter 5, forms primarily of top end socket 31, suction flange 32, inlet pressure sensing point 33, inlet guide pouring 34, outlet(discharge) flange 35, outlet guide pouring 36, outlet pressure sensing point 37, filter core 38 and top blow-down pipe 39.The operational condition of carbon monoxide in pressurized gas pipeline 2 is 1.6MPA, 40 DEG C, and the design condition of pressurized gas pipeline 2 is 1.85MPA, 40 DEG C.
The working principle of native system is:
In native system, after-filter 5 is connected on front filter 3 downstream, front filter 3 is first used during use, stop valve 7 now on front filter bypass line 4 is closed, the stop valve 7 that two ends imported and exported by after-filter 5 is closed, compression carbon monoxide is after front filter 3, then through this flow process of after-filter bypass line 6, original production status can normally be kept.
When front filter 3 pressure reduction is higher than 0.75bar, illustrate that the filter core of front filter 3 has blocking, when needing to keep in repair front filter 3, the stop valve 7 directly front filter 3 can being imported and exported two ends is closed, open the stop valve 7 on front filter bypass line 4, open the stop valve 7 that two ends imported and exported by after-filter 5, and the stop valve 7 of closing on after-filter bypass line 6, front filter 3 can be unloaded like this and carry out more renew cartridge or maintenance, play and remain normal and produce, again the object of more renew cartridge.
After front filter 3 maintenance process, normal mode can be switched to, both front filter 3 was arranged on pressurized gas pipeline 2, open the stop valve 7 that front filter 3 imports and exports two ends, stop valve 7 on front filter bypass line 4 is closed, the stop valve 7 that two ends imported and exported by after-filter 5 is opened, close the stop valve 7 on after-filter bypass line 6, compression carbon monoxide is through front filter 3, by the pattern of filter 5 later, to prevent after-filter 5 after pressure reduction raises, directly affect product pressure.
Claims (5)
1. can change the carbon monoxide compressor filtration system of filter by on-bne repair for one kind, the outlet of carbon monoxide compressor connects pressurized gas pipeline, this pressurized gas pipeline is provided with front filter, it is characterized in that, described pressurized gas pipeline is also provided with front filter bypass line, after-filter and after-filter bypass line, described after-filter and after-filter bypass line are located at the downstream of front filter, the import and export two ends of described front filter are provided with stop valve, and the import and export two ends of described after-filter are provided with stop valve; Described front filter bypass line and after-filter bypass line are equipped with stop valve.
2. according to claim 1ly a kind ofly can change the carbon monoxide compressor filtration system of filter by on-bne repair, it is characterized in that, the import and export of described front filter bypass line are positioned at the outside of the stop valve at the import and export two ends of front filter; The import and export of described after-filter bypass line are positioned at the outside of the stop valve at the import and export two ends of after-filter.
3. according to claim 1ly a kind ofly can change the carbon monoxide compressor filtration system of filter by on-bne repair, it is characterized in that, the both sides that front filter imports and exports the stop valve at two ends are all provided with blind plate; The both sides that the stop valve at two ends imported and exported by after-filter are all provided with blind plate.
4. according to claim 1ly a kind ofly can change the carbon monoxide compressor filtration system of filter by on-bne repair, it is characterized in that, described front filter and the top of after-filter are equipped with pressure relief valve.
5. according to claim 1ly a kind ofly can change the carbon monoxide compressor filtration system of filter by on-bne repair, it is characterized in that, described front filter and after-filter all adopt model to be the filter of bohr MCC1401E500H13.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106621615A (en) * | 2015-10-28 | 2017-05-10 | 上海华林工业气体有限公司 | CO filter for HYCO apparatus |
CN112717630A (en) * | 2020-12-31 | 2021-04-30 | 天脊煤化工集团股份有限公司 | Method for replacing adsorbent of adsorption tower on line |
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CN202342994U (en) * | 2011-10-13 | 2012-07-25 | 内蒙古伊利实业集团股份有限公司 | Filtering system for replacing filter element on line |
CN202611880U (en) * | 2012-06-13 | 2012-12-19 | 新乡市永新工业滤器有限公司 | Gas turbine coal gas inlet filtering device |
CN203717296U (en) * | 2014-01-27 | 2014-07-16 | 上海华林工业气体有限公司 | Carbon monoxide compressor filter system capable of online overhauling and replacing filter |
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2014
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Publication number | Priority date | Publication date | Assignee | Title |
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US20060123743A1 (en) * | 2004-12-10 | 2006-06-15 | Haldex Brake Products Gmbh | Cartridge for cleaning compressed air in compressed air supply systems of motor vehicles |
CN102008852A (en) * | 2010-10-15 | 2011-04-13 | 南通海鹰机电集团有限公司 | Online filtering device |
CN202185245U (en) * | 2011-07-18 | 2012-04-11 | 天津舜天达天然气有限公司 | Novel air compressor unit |
CN202223998U (en) * | 2011-08-26 | 2012-05-23 | 河南宝舜化工科技有限公司 | Gas filter device |
CN202342994U (en) * | 2011-10-13 | 2012-07-25 | 内蒙古伊利实业集团股份有限公司 | Filtering system for replacing filter element on line |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN106621615A (en) * | 2015-10-28 | 2017-05-10 | 上海华林工业气体有限公司 | CO filter for HYCO apparatus |
CN106621615B (en) * | 2015-10-28 | 2018-12-11 | 上海华林工业气体有限公司 | A kind of CO filter for HYCO device |
CN112717630A (en) * | 2020-12-31 | 2021-04-30 | 天脊煤化工集团股份有限公司 | Method for replacing adsorbent of adsorption tower on line |
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Application publication date: 20150729 |