CN218910255U - Crude synthesis gas purifying separator - Google Patents
Crude synthesis gas purifying separator Download PDFInfo
- Publication number
- CN218910255U CN218910255U CN202222773148.1U CN202222773148U CN218910255U CN 218910255 U CN218910255 U CN 218910255U CN 202222773148 U CN202222773148 U CN 202222773148U CN 218910255 U CN218910255 U CN 218910255U
- Authority
- CN
- China
- Prior art keywords
- synthesis gas
- separator
- crude synthesis
- inlet
- boiler water
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model discloses a crude synthesis gas purifying separator which comprises a supporting piece and a cylinder body positioned on the supporting piece, wherein an anti-collision baffle plate, a gas collector, a distribution pipe and a silk screen foam remover are sequentially arranged in the cylinder body from bottom to top. The device can remove solid dust of the crude synthesis gas, avoids the phenomenon of blocking downstream pipelines and valves caused by dust aggregation, ensures the safe operation of the device, and has good economic benefit.
Description
Technical Field
The utility model belongs to the technical field of chemical equipment, and relates to a crude synthesis gas purifying separator.
Background
In the coal chemical production, 2-5 mg/Nm of coarse synthesis gas of the coal gasification device is entrained 3 In order to prevent subsequent dust build-up from clogging the pipes and valves, the gas stream needs to be cleaned when entering the interface. It is common practice to pass the stream of raw synthesis gas through a gas-liquid separator and to separate it by gravity sedimentation, which generally removes part of the large-particle solid particles, but it is disadvantageous mainly in that it is difficult to completely remove the solid particles, especially small-particle dust, from the gas. Along with the operation of the device, small-particle dust is gradually accumulated, so that the phenomenon of pipeline blockage is caused, and the normal production of the device is influenced.
Disclosure of Invention
Aiming at the defects existing in the prior art, the utility model provides a crude synthesis gas purifying separator which can effectively remove solid particles in crude synthesis gas, avoid the risk of blocking downstream pipelines and valves and improve the operation period of the device.
In order to achieve the above purpose, the technical scheme adopted by the utility model is as follows:
the utility model provides a coarse synthesis gas purification separator, includes support piece, and is located barrel on the support piece, barrel inside is equipped with scour protection baffle, gas collector, distribution pipe and silk screen demister from bottom to top in proper order.
The technical scheme of the utility model is as follows: the outside of the gas collector is provided with a coil pipe, and a plurality of small holes are formed in the gas collector and the coil pipe.
The technical scheme of the utility model is as follows: the bottom of the cylinder is provided with a crude synthesis gas condensate outlet N3, the top of the cylinder is provided with a purified gas outlet N2, and the middle of the cylinder is provided with a crude synthesis gas inlet N1.
The technical scheme of the utility model is as follows: the upper part of the cylinder is provided with a first boiler water supply inlet N4 and a second boiler water supply inlet N5.
The technical scheme of the utility model is as follows: the distribution pipe inlet is connected with a second boiler water supply inlet N5, and the coil pipe inlet is connected with a first boiler water supply inlet N4.
The technical scheme of the utility model is as follows: the support piece is of a skirt structure.
The beneficial effects of the utility model are as follows: when the gas containing the solid dust enters the coarse synthesis gas purification separator and passes through the gas collector, most of the solid dust is removed by the boiler water sprayed by the coil pipe, a small amount of the solid dust is further removed under the spraying action of the boiler water in the distribution pipe, and the solid dust removal is realized through the wetting and cleaning actions of the boiler water, so that the phenomenon of blocking downstream pipelines and valves caused by dust aggregation is avoided, the safe operation of the device is ensured, and good economic benefits are realized.
Drawings
Fig. 1 is a schematic view of the overall structure of the present utility model.
In the figure: 1-supporting piece, 2-cylinder, 3-anti-flushing baffle, 4-collector, 5-distributor, 6-silk screen foam remover, N1-crude synthetic gas inlet, N2-purified gas outlet, N3-crude synthetic gas condensate outlet, N4-first boiler feed water inlet, N5-second boiler feed water inlet.
Detailed Description
The utility model will now be described in detail with reference to the drawings and specific examples.
As shown in FIG. 1, the crude synthesis gas purifying separator comprises a supporting piece and a cylinder body positioned on the supporting piece, wherein an anti-collision baffle, a gas collector, a distribution pipe and a silk screen demister are sequentially arranged in the cylinder body from bottom to top; the outer side of the gas collector is provided with a coil pipe, and the gas collector and the coil pipe are provided with a plurality of small holes; the bottom of the cylinder is provided with a crude synthesis gas condensate outlet N3, the top of the cylinder is provided with a purified gas outlet N2, and the middle of the cylinder is provided with a crude synthesis gas inlet N1; the upper part of the cylinder is provided with boiler water inlets N4 and N5; the distribution pipe inlet is connected with a first boiler water supply inlet N4, and the coil pipe inlet is connected with a second boiler water supply inlet N5; the support piece is of a skirt structure.
The working process of the utility model is as follows: the crude synthesis gas containing solid dust particles enters a barrel 2 of the separator from a crude synthesis gas inlet N1, collides with an anti-collision baffle 3, and a small amount of solids settle under the action of gravity and flow out from crude synthesis gas condensate N3; the crude synthesis gas containing most of solid dust enters the gas collector 4 and is removed by the boiler water sprayed from the coil pipe, a small amount of solid dust is further removed under the spraying action of the boiler water in the distribution pipe, and the solid dust removal target is realized through the wetting and cleaning actions of the boiler water.
The specific implementation process is as follows: 1000Nm 3 Raw synthesis gas/h (with a solids dust content of about 3 mg/Nm) 3 ) After entering a barrel body 2 of the separator and colliding with a shock-proof baffle 4, about 900mg/h of solid dust is settled under the action of gravity and flows out of a crude synthesis gas condensate N3; the crude synthesis gas containing most of the solid dust (about 2000 mg/h) enters the gas collector 4, is removed by the boiler water sprayed from the coil pipe, and a small amount of the solid dust (about 100 mg/h) is further removed under the spraying action of the boiler water in the distribution pipe, and finally, the solid dust is removed through the wetting and cleaning action of the boiler water, so that purified gas is obtained and sent to a downstream production unit.
The foregoing embodiments and description are merely illustrative of the principles of the present utility model, and are not intended to limit the scope of the utility model, which is susceptible to various changes and modifications without departing from the spirit and scope of the utility model, and these changes and modifications fall within the scope of the utility model as hereinafter claimed. The utility model is not related in part to the same as or can be practiced with the prior art.
Claims (5)
1. A raw synthesis gas purification separator, characterized by: the anti-collision device comprises a supporting piece (1) and a cylinder body (2) positioned on the supporting piece (1), wherein an anti-collision baffle (3), a gas collector (4), a distribution pipe (5) and a silk screen foam remover (6) are sequentially arranged in the cylinder body (2) from bottom to top; a coil pipe (7) is arranged on the outer side of the gas collector (4), and a plurality of small holes are formed in the gas collector (4) and the coil pipe (7).
2. The raw syngas clean-up separator of claim 1, wherein: the bottom of the cylinder body (2) is provided with a crude synthesis gas condensate outlet (N3), the top is provided with a purified gas outlet (N2), and the middle is provided with a crude synthesis gas inlet (N1).
3. The raw syngas clean-up separator of claim 1, wherein: the upper part of the cylinder body (2) is provided with a first boiler water supply inlet (N4) and a second boiler water supply inlet (N5).
4. The raw syngas clean-up separator of claim 1, wherein: the inlet of the distribution pipe (5) is connected with the second boiler water supply inlet (N5), and the inlet of the coil pipe (7) is connected with the first boiler water supply inlet (N4).
5. The raw syngas clean-up separator of claim 1, wherein: the support piece (1) is of a skirt structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202222773148.1U CN218910255U (en) | 2022-10-20 | 2022-10-20 | Crude synthesis gas purifying separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202222773148.1U CN218910255U (en) | 2022-10-20 | 2022-10-20 | Crude synthesis gas purifying separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN218910255U true CN218910255U (en) | 2023-04-25 |
Family
ID=86044574
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202222773148.1U Active CN218910255U (en) | 2022-10-20 | 2022-10-20 | Crude synthesis gas purifying separator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN218910255U (en) |
-
2022
- 2022-10-20 CN CN202222773148.1U patent/CN218910255U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202786150U (en) | Chilling washing system for raw gas gasified by dry pulverized coal | |
CN102690689B (en) | Device and method for scrubbing and purifying coal gas | |
CN104073296A (en) | Technology and device for dust removal purification of IGCC (Integrated gasification combined cycle) raw gas | |
CN101721175B (en) | Bag type dust collector with novel air inlet mode and airflow distribution structure | |
CN105268268B (en) | A kind of Vertical Combination high-efficiency desulfurization deamination dust arrester | |
CN102586523B (en) | Blast furnace gas purification plant | |
CN218910255U (en) | Crude synthesis gas purifying separator | |
CN208472004U (en) | A kind of cleaning dust device of synthesis gas | |
CN112442395A (en) | Water coal slurry gasification coarse gas washing tower | |
CN110237630A (en) | A kind of big liquid-gas ratio multilayer step dedusting demisting packed tower | |
CN105062574A (en) | Efficient combined dusty syngas washing dust removal device and method thereof | |
CN204958841U (en) | Efficient combination formula dust -laden synthetic gas washing dust collector | |
CN103060017B (en) | Combined spiral tower tray for gas washing tower, gas cleaning device and application thereof | |
CN115193202A (en) | Energy-saving environment-friendly synthetic gas washing tower | |
CN208553531U (en) | A kind of the mixer wash mill and mixer washing system of dust-laden synthesis gas | |
CN203128516U (en) | Combined washing apparatus | |
CN202595069U (en) | Coal gas scrubbing and purifying device | |
CN109628161B (en) | Washing tower with built-in cyclone and air guide plate group | |
CN202315599U (en) | Water bath dust removing system | |
CN213570349U (en) | Coal ash separator of gasifier | |
CN220951683U (en) | Coke oven gas combined demisting and dedusting device | |
CN206385102U (en) | A kind of dedusting dehydrating tower | |
CN207362161U (en) | A kind of synthesis gas fine purifiation device | |
CN205133531U (en) | Washing tower structure | |
CN106520217A (en) | Dust removal dehydration tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |