CN107161949A - One kind synthesis cyclonic current takes off hydrocarbon device - Google Patents
One kind synthesis cyclonic current takes off hydrocarbon device Download PDFInfo
- Publication number
- CN107161949A CN107161949A CN201710372204.1A CN201710372204A CN107161949A CN 107161949 A CN107161949 A CN 107161949A CN 201710372204 A CN201710372204 A CN 201710372204A CN 107161949 A CN107161949 A CN 107161949A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- synthesis
- cyclone pipe
- ring surface
- outer ring
- 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.)
- Pending
Links
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 30
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 30
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 18
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 18
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 238000000926 separation method Methods 0.000 claims abstract description 10
- 238000009434 installation Methods 0.000 claims description 13
- 239000012530 fluid Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 5
- 229960004424 carbon dioxide Drugs 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/24—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/702—Hydrocarbons
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
Abstract
Hydrocarbon device, including cylinder, at least one cyclone pipe for gas-liquid separation for being vertically arranged in the cylinder internal upper part are taken off the invention discloses one kind synthesis cyclonic current, the cyclone pipe is fixed on the cylinder inboard wall by a fixation kit；A synthesis gas entrance is provided with the top of the cylinder, the cyclone pipe medium position is provided with a syngas outlet in the cylinder outer ring surface；The cylinder body bottom is provided with a condensate outlet.The present invention sets fixation kit to fix cyclone pipe in inner barrel, and cyclone pipe carries out gas-liquid separation to the synthesis gas of inner barrel, and the synthesis gas after separation is gone out from top, liquid is gone out from the condensate outlet of bottom, is realized gas-liquid and is preferably separated.
Description
Technical field
The present invention relates to synthesis gas processing technology field, relate generally to a kind of synthesis cyclonic current and take off hydrocarbon device.
Background technology
Synthesis gas is a kind of unstripped gas as industrial chemicals using carbon monoxide and hydrogen as key component.Synthesis gas
Raw material range is very wide, can be produced by the solid fuel gasification such as coal or coke, also can be by the light hydrocarbons system such as natural gas and naphtha
Take, can also be produced by heavy oil partial oxidation method.When being produced by the light hydrocarbons such as natural gas and naphtha, two in natural gas
The sour gas such as carbonoxide, hydrogen sulfide can contact to form corrosivity acid solution with vapor, cause the corrosion of pipeline；In synthesis gas
Carbon monoxide and hydrogen are imflammable gas, and easily with the oxygen reaction generation carbon dioxide and water in air, carbon dioxide is again
It is greenhouse effects main cause, it is necessary to which gas is separated with liquid, improves the purifying rate of hydrocarbon impurity.
The content of the invention
The technical problems to be solved by the invention are to provide one kind and set cyclone pipe to carry out gas-liquid to synthesis gas in cylinder
Separation, improves the purifying rate of hydrocarbon impurity, and synthesis cyclonic current simple in construction, easy to use takes off hydrocarbon device.
The technical problems to be solved by the invention can adopt the following technical scheme that to realize：
One kind synthesis cyclonic current takes off hydrocarbon device, it is characterised in that including cylinder, be vertically arranged in the cylinder internal upper part extremely
Few one is used for the cyclone pipe of gas-liquid separation, and the cyclone pipe is fixed on the cylinder inboard wall by a fixation kit；In the cylinder
A synthesis gas entrance is provided with the top of body, the cyclone pipe medium position, which is provided with a synthesis gas, in the cylinder outer ring surface goes out
Mouthful；The cylinder body bottom is provided with a condensate outlet.
In a preferred embodiment of the invention, the fixation kit includes being horizontally installed on the cylinder internal upper part
Lower perforated plate on a pair；In the cylinder body outer wall the first installation base, the upper pipe are respectively outward extended with the upper perforated plate two ends
Plate two ends stretch out the cylinder body outer wall and respectively set a shaft shoulder stud to be fixed with first installation base；The lower perforated plate two ends
It is welded on the cylinder inboard wall.
In a preferred embodiment of the invention, the cyclone pipe is a pair be symmetrical set, the cyclone pipe
Including central tube and the outer barrel being arranged on the outside of the central tube, the outer barrel includes overflow segment, the circle from top to bottom set
Column body segment, cone section and desilting section；Rotary fluid is provided with the outside of the overflow segment, is set in the rotary fluid outer ring surface
There is the rotational flow inlet of taper；
The outer ring surface upper and lower side annular of the central tube is provided with locating ring, at the top of the locating ring outer ring surface or bottom
Portion is provided with ring-shaped step, if be vertically arranged with the central tube side bolt stem be fixed on through the ring-shaped step it is described
On a pair on lower perforated plate.
In a preferred embodiment of the invention, the cylinder top is set to ellipse head, in the ellipse head
On be provided with drain；The cylinder bottom is set to arch back cover, and the cylinder body bottom is provided with skirt；
2 liquid level connected entrances are provided with the cylinder outer ring surface lower end thereof is longitudinally spaced, in the cylinder outer ring surface
The bottom other end is provided with 2 liquid levels regulation mouths in the liquid level connected entrance relevant position is longitudinally spaced.
In a preferred embodiment of the invention, long-neck W.N flange is provided at both ends with the middle part of the cylinder body outer wall,
The second installation base is respectively outward extended with the long-neck W.N flange, one is vertically arranged with second installation base
Stud, the stud two ends respectively set a nut to fasten.
The beneficial effects of the invention are as follows：One kind synthesis cyclonic current takes off hydrocarbon device, and fixation kit is set by eddy flow in inner barrel
Pipe is fixed, and cyclone pipe carries out gas-liquid separation to the synthesis gas of inner barrel, and the synthesis gas after separation is gone out from top, liquid is the bottom of from
The condensate outlet in portion is gone out, and is realized gas-liquid and is preferably separated；Cyclone pipe is longitudinally disposed a pair, passes through the one of laterally setting
The inwall of cylinder is fixed on to tube sheet, comprehensive gas-liquid separation preferably can be carried out to synthesis gas, improve separative efficiency.
Brief description of the drawings
Fig. 1, which is that the present invention is a kind of, synthesizes the structural representation that cyclonic current takes off hydrocarbon device.
Fig. 2 is enlarged drawing at A in Fig. 1 of the present invention.
Embodiment
In order that the technical means, the inventive features, the objects and the advantages of the present invention are easy to understand, tie below
Conjunction is specifically illustrating, and the present invention is expanded on further.
Referring to Fig. 1 to Fig. 2, what is provided in figure is that a kind of synthesis cyclonic current takes off hydrocarbon device, including cylinder 100, is vertically arranged in
At least the one of the internal upper part of cylinder 100 is used for the cyclone pipe 200 of gas-liquid separation, and cyclone pipe 200 is a pair be symmetrical set；Rotation
Flow tube 200 is fixed on the inwall of cylinder 100 by a fixation kit 300, and fixation kit 300 includes being horizontally installed in cylinder 100
Lower perforated plate 310 in a pair of top.
The top of cylinder 100 is provided with a synthesis gas entrance 110, in the outer ring surface of cylinder 100 in the medium position of cyclone pipe 200
A syngas outlet 120 is provided with, one is provided between synthesis gas entrance 110, syngas outlet 120 and the outer wall of cylinder 100 and is added
Strong pipe 111,121；The bottom of cylinder 100 is provided with a condensate outlet 130, L-type pipeline 131 is provided with condensate outlet 130,
The end of L-type pipeline 131 is provided with lime set adapter 132.
In the outer wall of cylinder 100 the first installation base 320, upper perforated plate 311 are respectively outward extended with the left and right ends of upper perforated plate 311
Two ends stretch out the outer wall of cylinder 100 and are stuck in the middle part of the first installation base 320, and a shaft shoulder stud is set on the first installation base 320
330 fix upper perforated plate 311 with the first installation base 320；The left and right ends of lower perforated plate 312 are welded on the inwall of cylinder 100.
Cyclone pipe 200 includes the outer barrel 220 in central tube 210 and the outside of centrally disposed pipe 210, outer barrel 220 include by
Overflow segment 221, shell portion 222, cone section 223 and the desilting section 224 of upper and lower setting；Set in the outside of overflow segment 221
Rotary fluid 225 is equipped with, the outer ring surface of rotary fluid 225 is provided with the rotational flow inlet 226 of taper.
The outer ring surface upper end annular of central tube 210 is provided with the first locating ring 211, in the outer ring surface of the first locating ring 211
Top annular is provided with first annular step 212；The outer ring surface lower end annular of central tube 210 is provided with the second locating ring,
Second locating ring outer ring surface base circle is provided with the second ring-shaped step；If being vertically arranged with bolt stem in the side of central tube 210
213 are fixed on lower perforated plate 311,312 through first annular step 212, the second ring-shaped step.
The top of cylinder 100 is set to ellipse head 140, and drain 141 is provided with ellipse head 140；The bottom of cylinder 100
End is set to arch back cover 150, and the bottom of cylinder 100 is provided with skirt 160；Between the outer ring surface lower end thereof longitudinal direction of cylinder 100
Every being provided with 2 liquid level connected entrances 170, in the outer ring surface bottom other end of cylinder 100 in the relevant position of liquid level connected entrance 170 longitudinal direction
It is arranged at intervals with 2 liquid level regulation mouths 180
Long-neck W.N flange 190 is provided at both ends with the middle part of the outer wall of cylinder 100, it is each outside on long-neck W.N flange 190
The second installation base 191 is extended with, a stud 192 is vertically arranged with the second installation base 191, the two ends of stud 192 are respectively set
A nut 193 is put to fasten.
General principle, principal character and the advantages of the present invention of the present invention has been shown and described above.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the simply explanation described in above-described embodiment and specification is originally
The principle of invention, various changes and modifications of the present invention are possible without departing from the spirit and scope of the present invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention is by appended claims and together
Defined Deng thing.
Claims (5)
1. one kind synthesis cyclonic current takes off hydrocarbon device, it is characterised in that including cylinder, be vertically arranged in the cylinder internal upper part at least
One is used for the cyclone pipe of gas-liquid separation, and the cyclone pipe is fixed on the cylinder inboard wall by a fixation kit；In the cylinder
Top is provided with a synthesis gas entrance, and the cyclone pipe medium position, which is provided with a synthesis gas, in the cylinder outer ring surface goes out
Mouthful；The cylinder body bottom is provided with a condensate outlet.
2. a kind of synthesis cyclonic current as claimed in claim 1 takes off hydrocarbon device, it is characterised in that the fixation kit includes laterally setting
Put the lower perforated plate in a pair of the cylinder internal upper part；In the cylinder body outer wall is respectively outward extended with the upper perforated plate two ends
One installation base, the upper perforated plate two ends stretch out the cylinder body outer wall and respectively set a shaft shoulder stud and first installation base
It is fixed；The lower perforated plate two ends are welded on the cylinder inboard wall.
3. a kind of synthesis cyclonic current as claimed in claim 2 takes off hydrocarbon device, it is characterised in that the cyclone pipe sets to be symmetrical
A pair put, the cyclone pipe includes central tube and the outer barrel being arranged on the outside of the central tube, and the outer barrel is included by upper
And overflow segment, shell portion, cone section and the desilting section of lower setting；Rotary fluid is provided with the outside of the overflow segment,
The rotary fluid outer ring surface is provided with the rotational flow inlet of taper；
The outer ring surface upper and lower side annular of the central tube is provided with locating ring, at the top of the locating ring outer ring surface or bottom is set
Be equipped with ring-shaped step, if be vertically arranged with the central tube side bolt stem be fixed on through the ring-shaped step it is the pair of
On upper lower perforated plate.
4. a kind of synthesis cyclonic current as claimed in claim 1 takes off hydrocarbon device, it is characterised in that the cylinder top is set to ellipse
End socket, drain is provided with the ellipse head；The cylinder bottom is set to arch back cover, is set in the cylinder body bottom
It is equipped with skirt；
2 liquid level connected entrances are provided with the cylinder outer ring surface lower end thereof is longitudinally spaced, in the cylinder outer ring surface bottom
The other end is provided with 2 liquid levels regulation mouths in the liquid level connected entrance relevant position is longitudinally spaced.
5. a kind of synthesis cyclonic current as claimed in claim 1 takes off hydrocarbon device, it is characterised in that the two ends in the middle part of the cylinder body outer wall
Long-neck W.N flange is provided with, the second installation base is respectively outward extended with the long-neck W.N flange, in the described second peace
A stud is vertically arranged with dress boss, the stud two ends respectively set a nut to fasten.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710372204.1A CN107161949A (en) | 2017-05-23 | 2017-05-23 | One kind synthesis cyclonic current takes off hydrocarbon device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710372204.1A CN107161949A (en) | 2017-05-23 | 2017-05-23 | One kind synthesis cyclonic current takes off hydrocarbon device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107161949A true CN107161949A (en) | 2017-09-15 |
Family
ID=59821810
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710372204.1A Pending CN107161949A (en) | 2017-05-23 | 2017-05-23 | One kind synthesis cyclonic current takes off hydrocarbon device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107161949A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU1380992A (en) * | 1991-04-19 | 1992-10-22 | Outokumpu Research Oy | Multigas scrubber |
| CN101703384A (en) * | 2005-05-27 | 2010-05-12 | 戴森技术有限公司 | Cyclonic separating apparatus |
| CN102198353A (en) * | 2011-02-28 | 2011-09-28 | 西安石油大学 | Gas-liquid separation pipe and combined adjustable gas-liquid separation apparatus |
| CN102380262A (en) * | 2010-09-01 | 2012-03-21 | 中国石油化工股份有限公司 | High-pressure separator and method for high-pressure separation |
| CN102430294A (en) * | 2011-09-08 | 2012-05-02 | 上海华畅环保设备发展有限公司 | Micro-cyclone reinforced separation device and method for cold-high-pressure separator |
| CN202808742U (en) * | 2012-10-29 | 2013-03-20 | 中国石油天然气集团公司 | Spiral-flow type natural gas dehydration device |
-
2017
- 2017-05-23 CN CN201710372204.1A patent/CN107161949A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU1380992A (en) * | 1991-04-19 | 1992-10-22 | Outokumpu Research Oy | Multigas scrubber |
| CN101703384A (en) * | 2005-05-27 | 2010-05-12 | 戴森技术有限公司 | Cyclonic separating apparatus |
| CN102380262A (en) * | 2010-09-01 | 2012-03-21 | 中国石油化工股份有限公司 | High-pressure separator and method for high-pressure separation |
| CN102198353A (en) * | 2011-02-28 | 2011-09-28 | 西安石油大学 | Gas-liquid separation pipe and combined adjustable gas-liquid separation apparatus |
| CN102430294A (en) * | 2011-09-08 | 2012-05-02 | 上海华畅环保设备发展有限公司 | Micro-cyclone reinforced separation device and method for cold-high-pressure separator |
| CN202808742U (en) * | 2012-10-29 | 2013-03-20 | 中国石油天然气集团公司 | Spiral-flow type natural gas dehydration device |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170915 |
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| WD01 | Invention patent application deemed withdrawn after publication |