CN208829616U - Remove the process system of carbon dioxide in natural - Google Patents
Remove the process system of carbon dioxide in natural Download PDFInfo
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- CN208829616U CN208829616U CN201820991189.9U CN201820991189U CN208829616U CN 208829616 U CN208829616 U CN 208829616U CN 201820991189 U CN201820991189 U CN 201820991189U CN 208829616 U CN208829616 U CN 208829616U
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- adsorption tower
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- 238000000034 method Methods 0.000 title claims abstract description 57
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 55
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 55
- 239000007789 gas Substances 0.000 claims abstract description 77
- 239000003345 natural gas Substances 0.000 claims abstract description 52
- 238000007664 blowing Methods 0.000 claims abstract description 27
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 230000008929 regeneration Effects 0.000 claims description 30
- 238000011069 regeneration method Methods 0.000 claims description 30
- 239000002808 molecular sieve Substances 0.000 claims description 17
- 239000002737 fuel gas Substances 0.000 claims description 10
- 238000000746 purification Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N AI2O3 Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 claims 1
- 239000003292 glue Substances 0.000 claims 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims 1
- 229910052710 silicon Inorganic materials 0.000 claims 1
- 239000010703 silicon Substances 0.000 claims 1
- ZZVUWRFHKOJYTH-UHFFFAOYSA-N Diphenhydramine Chemical compound C=1C=CC=CC=1C(OCCN(C)C)C1=CC=CC=C1 ZZVUWRFHKOJYTH-UHFFFAOYSA-N 0.000 abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 230000002588 toxic Effects 0.000 abstract description 3
- 231100000331 toxic Toxicity 0.000 abstract description 3
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 description 18
- 238000010521 absorption reaction Methods 0.000 description 13
- 239000000446 fuel Substances 0.000 description 12
- 239000004215 Carbon black (E152) Substances 0.000 description 7
- 238000001816 cooling Methods 0.000 description 7
- 150000002430 hydrocarbons Chemical class 0.000 description 7
- PVXVWWANJIWJOO-UHFFFAOYSA-N Methylenedioxyethylamphetamine Chemical compound CCNC(C)CC1=CC=C2OCOC2=C1 PVXVWWANJIWJOO-UHFFFAOYSA-N 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 230000000274 adsorptive Effects 0.000 description 3
- 206010002855 Anxiety Diseases 0.000 description 2
- 206010057666 Anxiety disease Diseases 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 230000036506 anxiety Effects 0.000 description 2
- 238000005262 decarbonization Methods 0.000 description 2
- 238000005261 decarburization Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000000741 silica gel Substances 0.000 description 2
- 229910002027 silica gel Inorganic materials 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000001351 cycling Effects 0.000 description 1
- 230000004059 degradation Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001681 protective Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000001502 supplementation Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Abstract
Remove the process system of carbon dioxide in natural.Traditional wet process removes carbon dioxide in natural, and process is complicated, and equipment is various, and hydramine reagent is toxic, and make-up solution and desalted water are needed in operation.The utility model composition includes: raw natural gas entrance, it is characterized in that: raw natural gas entrance by valve respectively with adsorption tower A(1), adsorption tower B(2), adsorption tower C(3) inlet tube connection, adsorption tower A, adsorption tower B, the outlet of adsorption tower C is connect by valve with purified natural gas pipe, purified natural gas pipe is connected by valve with each cold blowing inlet tube, each cold blowing outlet is connected with cold blowing Gas Cooler (7) inlet tube, cold blowing Gas Cooler outlet is connected with purified natural gas pipe, heater (5) outlet by valve respectively with adsorption tower A, adsorption tower B, adsorption tower C inlet tube is connected, circularly-supercharged machine outlet is connected with heater inlet pipe.The utility model is used to remove the process system of carbon dioxide in natural.
Description
Technical field:
The utility model relates to the natural gas preconditioning technique fields in liquefaction Technology of Natural Gas, and in particular to a kind of removing
The process system of carbon dioxide in natural.
Background technique:
Natural gas is a kind of environmentally protective, economical and practical, safe and reliable high-grade energy, develops gas industry, naturally
The research of gas purifying process is also particularly important in gas liquefaction technology, because of the relatively high-solidification point component such as titanium dioxide in natural gas
Carbon, moisture and heavy hydrocarbon etc. can solidify in gas deliquescence process and occluding device, it is necessary to be removed before liquefaction；Tradition
Wet process remove carbon dioxide in natural, process is complicated, and equipment is various, and hydramine reagent is toxic, needs to supplement in operation molten
Liquid and desalted water.
Natural gas carbon dioxide removal processing method can be divided into wet process and two kinds of dry method, the development of wet process carbon dioxide removal more at
Ripe and application is more for hydramine method, hydramine method have absorb, regenerated technique removing precision is relatively high, treating capacity is big, natural
The advantages that gas methane high income, meets requirement of the LNG device to purified gas, but hydramine method process is complicated, and equipment is various, hydramine examination
Agent is toxic, and needs make-up solution and desalted water in operation, and carbon dioxide removal process need to be separately positioned with dehydration procedure, for
The regional applicability of water shortage or land used anxiety is bad；It can reach naturally in dry method carbon dioxide removal using temp.-change adsorptive process (TSA)
Qi exhaustion carbon dioxide, dehydration and de- heavy hydrocarbon purpose, have process it is simple, it is easy to operate, corrosion-free and pollution, occupied area it is small,
The low equal remarkable advantages of operating cost, but when single utilization routine temp.-change adsorptive process, because carbon dioxide is different from moisture in regeneration gas
And heavy hydrocarbon, it can not be separated after cooling, cause this partial regeneration gas that can not recycle, be original with maximum resource utilization
Then, regeneration gas can be used as distributed energy power generation.But in the occasion for not using distributed energy, this partial regeneration gas is wasted
Fall, causes the LNG device natural gas methane rate of recovery not high, therefore conventional dry decarburization is not particularly suited for not using distributed energy
The occasion in source.
Utility model content:
The purpose of the utility model is to provide a kind of process system for removing carbon dioxide in natural, system is simple, suitable
With property is strong, methane recovery is high, technique using three towers (can also according to circumstances use two towers) temp.-changing adsorption (TSA) with it is circularly-supercharged
Machine serial flow removes carbon dioxide in natural gas or other impurities.
Above-mentioned purpose is realized by following technical scheme:
A kind of process system removing carbon dioxide in natural, composition includes: raw natural gas entrance, the original
Material gas inlet is connect with the inlet tube of adsorption tower A, adsorption tower B, adsorption tower C respectively by valve, adsorption tower A, adsorption tower
B, the outlet of adsorption tower C is connect by valve with purified natural gas pipe, and purified natural gas pipe passes through valve and each cold blowing import
Pipe is connected, and each cold blowing outlet is connected with cold blowing Gas Cooler inlet tube, cold blowing Gas Cooler outlet and purified natural gas pipe
It is connected, heater outlet pipe is connected with adsorption tower A, adsorption tower B, adsorption tower C inlet tube respectively by valve, adsorption tower A, absorption
The outlet tower B, adsorption tower C stove pipe is connected by valve with storage heater inlet tube, accumulator outlet pipe and circularly-supercharged machine into
Mouth pipe is connected, and circularly-supercharged machine outlet is connected with heater inlet pipe.
The process system of the removing carbon dioxide in natural, the accumulator outlet pipe pass through valve and fuel
The connection of gas surge tank inlet tube, the fuel gas surge tank outlet are connect with fuel gas pipe, and adsorption tower is de- in temperature-rise period
A small amount of mixed gas of the carbon dioxide and natural gas that remove is as fuel.
The process system of the removing carbon dioxide in natural, the accumulator outlet pipe and regeneration Gas Cooler
Inlet tube connection, the regeneration gas cooler outlet pipe are connect by valve with the raw natural gas pipe, and described follows
Ring supercharger import is arranged purified gas and supplements pipeline.
The process system of the removing carbon dioxide in natural, it is the adsorption tower A, the adsorption tower B, described
Adsorption tower C filler be molecular sieve, molecular sieve and active carbon multiple-hearth, molecular sieve and silica gel multiple-hearth or molecular sieve and active oxygen
Change aluminium combination.
The utility model has the advantages that
1. the utility model is mainly to provide a kind of process system for removing carbon dioxide in natural, it is suitable for various days
Right gas source, is particularly suitable for the less situation of carbon dioxide in natural gas content, solves and do not use distributed energy
When routine temp.-change adsorptive process carbon dioxide removal can not efficiently use regeneration gas problem.
For the utility model mainly for the area of water shortage or land used anxiety, applicability is good, the recycling of LNG device natural gas methane
Rate is high, while process of the invention is simple, investment is small, environmentally friendly, occupied area is small, has many advantages, such as easy to operate.
The utility model is increased in order to solve the problems, such as that regeneration gas is irretrievable in absorption method technique, by regeneration gas by circulation
Press is by regeneration gas circulating-heating, so that absorption tower packing heating, increases precipitation with temperature in adsorption tower during heating
Natural gas containing carbon dioxide enters fuel surge tank, lets out the adsorption tower in heated condition when heating closes to an end
Adsorption tower is included foreign gas and leaks into fuel surge tank by pressure, and absorption tower pressure interior force is only slightly higher than fuel surge tank, rises again later
Pressure, this measure greatly reduce out the flow of system regeneration gas, and the adsorption tower in heated condition after boosting still remains a small amount of
The impurity such as carbon dioxide restart circulating-heating process and heat gas are imported regeneration to reach further purification purpose
Raw material tracheae is incorporated to after Gas Cooler is cooling and enters adsorption process, to ensure that these fraction of impure gases will not be in cold blowing
Bring next procedure in journey into.
Detailed description of the invention:
Attached drawing 1 is the flowage structure schematic diagram of the utility model.
Wherein: 1, adsorption tower A, 2, adsorption tower B, 3, adsorption tower C, 4, circularly-supercharged machine, 5, heater, 6, accumulation of heat
Device, 7, cold blowing Gas Cooler, 8, regeneration Gas Cooler, 9, fuel gas surge tank.
Specific embodiment:
Embodiment 1:
A kind of process system removing carbon dioxide in natural, composition includes: raw natural gas entrance, the original
Material gas inlet is connect with the inlet tube of adsorption tower A1, adsorption tower B2, adsorption tower C3 respectively by valve, adsorption tower A, absorption
Tower B, adsorption tower C outlet connect with purified natural gas pipe by valve, purified natural gas pipe pass through valve and each cold blowing into
Mouth pipe is connected, and each cold blowing outlet is connected with 7 inlet tube of cold blowing Gas Cooler, cold blowing Gas Cooler outlet and purified natural gas
Pipe is connected, and 5 outlet of heater is connected with adsorption tower A, adsorption tower B, adsorption tower C inlet tube respectively by valve, adsorption tower A,
The outlet adsorption tower B, adsorption tower C stove pipe is connected by valve with 6 inlet tube of storage heater, accumulator outlet pipe with it is circularly-supercharged
4 inlet tube of machine is connected, and circularly-supercharged machine outlet is connected with heater inlet pipe.
Embodiment 2:
According to a kind of process system for removing carbon dioxide in natural described in embodiment 1, the accumulator outlet
Pipe is connect by valve with 9 inlet tube of fuel gas surge tank, and the fuel gas surge tank outlet is connect with fuel gas pipe, is risen
A small amount of mixed gas of adsorption tower removes during temperature carbon dioxide and natural gas is as fuel.
Embodiment 3:
According to a kind of process system for removing carbon dioxide in natural as described in example 2, the accumulator outlet
Pipe is connect with regeneration 8 inlet tube of Gas Cooler, and the regeneration gas cooler outlet pipe is natural by valve and the raw material
Tracheae connection, the circularly-supercharged machine import setting purified gas supplement pipeline.
Embodiment 4:
A kind of process system of removing carbon dioxide in natural according to embodiment 2 or 3, the adsorption tower A,
The adsorption tower B, the adsorption tower C filler are that molecular sieve, molecular sieve and active carbon multiple-hearth, molecular sieve and silica gel are compound
Bed or molecular sieve and other combination of adsorbents, are not limited to other fillers.
Embodiment 5:
The method of the process system of the removing carbon dioxide in natural according to one of embodiment 1-4, party's genealogy of law
System includes the following steps:
The source of raw natural gas is suitable for various natural gases first, is particularly suitable for carbon dioxide in natural gas
The less situation of content, using titanium dioxide in two towers or three tower temp.-changing adsorptions and circularly-supercharged machine serial flow removing natural gas
Carbon；
When using three tower temp.-changing adsorptions and when circularly-supercharged machine serial flow, accumulator outlet pipe and regeneration Gas Cooler into
Mouthful pipe is connected, and regeneration gas cooler outlet pipe is connected by valve with raw natural gas pipe, when adsorption tower A be in adsorbed state,
When adsorption tower B is in cold blowing state, adsorption tower C is in heated condition, and circularly-supercharged machine starts adsorption tower C and storage heater, adds
Natural gas adsorption closed cycle heating in hot device, prevents adsorption tower C pressure superelevation, portion of natural gas after heating temperature raising
It is discharged into fuel gas surge tank after storage heater, stops circularly-supercharged machine when closing to an end heating cycle and runs and close
Air intake valve in heated condition adsorption tower C；In heated condition adsorption tower C pressure release to the pressure of a little higher than fuel surge tank
Power, the interior gas rich in impurity of adsorption tower C open adsorption tower C air intake valve after being largely discharged and boost, this process reduces suction
Impurity content in attached tower in gas；
After adsorption tower C boosts, and before system switching in a bit of time, (a bit of time is
According in raw natural gas carbon dioxide content and unit scale determine；) rerun circularly-supercharged machine, adsorption tower C after
Continuous to be in heated condition, circularly-supercharged machine import setting cold blowing gas supplements pipeline, for the purified gas when heating closes to an end
Gas in displacement sorption tower, these gases for containing residual carbon dioxide return to raw natural gas after regeneration Gas Cooler is cooling
Inlet pipeline enters adsorption tower A circulation absorption；Under avoiding the carbon dioxide that residual is excessive in next cold blowing stage cylinder from taking to
A process；Adsorption tower C initially enters the cold blowing stage at the end of heating while adsorption tower B is in adsorbed state, and adsorption tower A is in
Heated condition；When cold blowing using Partial cleansing gas by adsorbent in adsorption tower is cooling and cold blowing gas is cooled to by cold blowing Gas Cooler
Enter next procedure after room temperature；When calculating determining cold blowing gas flow more than purification gas flow, can be increased using circulation
Press cooling mode；
When needing biggish demand for fuel, continuous supplementation purification gas during circulating-heating can be at the end of heating
Carbon dioxide in medium in adsorption tower C is diluted to and is met the requirements, then adsorption tower is not necessarily to pressure release and boost process；Described is de-
Except the process system of carbon dioxide in natural, the carbon dioxide in raw natural gas can be not only removed, original can also be removed
Expect the heavy hydrocarbon and moisture in natural gas；
This system can not only remove the carbon dioxide in raw natural gas, can also remove raw material it is natural in other are miscellaneous
Matter such as heavy hydrocarbon and moisture, but two sets of systems should be separated into, using same removal methods, heavy hydrocarbon and moisture are first removed, after
Carbon dioxide removal, though this is because circular regeneration gas temperature is higher, moisture therein still can by the micro absorption of molecular sieve from
And remaining moisture will affect the next period to the adsorption effect of carbon dioxide；
The more traditional wet process decarbonization system of the application, process is simple, equipment is few, project cost is low, easy to operate, traditional
Natural gas liquefaction device pretreatment system, decarbonization system mostly use greatly active MDEA technique, and MDEA method uses 45%~50%
MDEA aqueous solution, and add suitable activator to improve the absorption rate of carbon dioxide, MDEA is not degradable, have compared with
Strong anti-chemically and thermally degradation capability, it is current that corrosivity is small, and steam forces down, and solution cycling rate is low, and hydrocarbon solvability is small
Most widely used gas purification handles solvent, especially when in raw natural gas carbon dioxide content it is higher (typically larger than 1%)
When, which has wide range of applications, and domestic almost all of natural gas liquefaction engineering is all made of MDEA technique at present, though the technique
So there is degree of purification height, outstanding advantages of methane losses are small, but complex process, take up a large area, invest it is larger, for day
The lower situation of carbon dioxide content in right gas, the method carbon dioxide removal that can also be adsorbed using molecular sieve, but it is traditional
Molecular sieve absorbing process for the regeneration gas containing carbon dioxide can only be used as generator or gas turbine fuel because carbon containing
Regeneration gas only can not can only adapt to carbon dioxide separation, absorption method to use distributed energy unlike dehydration regeneration gas by cooling
Occasion, thus limit the use scope of absorption method, it is no matter former for not using the natural gas liquefaction plant of distributed energy
Expect carbon dioxide in natural content height, can only use traditional MDEA decarburization+molecular sieve dehydration technique.
In order to solve the problems, such as that regeneration gas is irretrievable in absorption method technique, regeneration gas is by circularly-supercharged machine by regeneration gas
Circulating-heating, so that absorption tower packing heating, contains carbon dioxide with what temperature raising was precipitated in adsorption tower during heating
Natural gas enter fuel surge tank, heating close to an end when will be in heated condition adsorption tower pressure release, will be in adsorption tower
Impure gas leaks into fuel surge tank, and absorption tower pressure interior force is only slightly higher than fuel surge tank, boosts again later, this measure subtracts significantly
The flow of system regeneration gas out is lacked, it is miscellaneous that the adsorption tower in heated condition after boosting still remains a small amount of carbon dioxide etc.
Matter supplements a small amount of purified gas restarting circulating-heating process and imports heat gas again to reach further purification purpose
Raw material tracheae is incorporated to after angry cooler is cooling and enters adsorption process, to ensure that these fraction of impure gases will not be in cold blowing
Bring subsequent processing into the process；
The application goes out that system regeneration throughput is small, and a small amount of regeneration gas can be used as molecular sieve heating and warming is used,
It is particularly suitable for not using the lower natural gas liquefaction device of the carbon dioxide content of distributed energy；
With 100 × 104Nm3For/d natural gas liquefaction engineering (it is assumed that carbon dioxide content 0.6% in unstripped gas), this is practical
It is novel as follows compared with traditional handicraft:
Claims (2)
1. a kind of process system for removing carbon dioxide in natural, composition includes: raw natural gas entrance, it is characterized in that:
The raw natural gas entrance is connect with the inlet tube of adsorption tower A, adsorption tower B, adsorption tower C respectively by valve, adsorption tower
A, the outlet of adsorption tower B, adsorption tower C connects by valve with purified natural gas pipe, purified natural gas pipe by valve with respectively
Cold blowing inlet tube is connected, and each cold blowing outlet is connected with cold blowing Gas Cooler inlet tube, cold blowing Gas Cooler outlet and purification
Natural gas tube is connected, and heater outlet pipe is connected with adsorption tower A, adsorption tower B, adsorption tower C inlet tube respectively by valve, adsorbs
Tower A, adsorption tower B, adsorption tower C outlet stove pipe are connected by valve with storage heater inlet tube, accumulator outlet pipe and circulation
Supercharger inlet tube is connected, and circularly-supercharged machine outlet is connected with heater inlet pipe；
The accumulator outlet pipe is connect by valve with fuel gas surge tank inlet tube, the fuel gas surge tank outlet
Pipe is connect with fuel gas pipe, and a small amount of mixed gas of adsorption tower removes in temperature-rise period carbon dioxide and natural gas is as combustion
Material；
The accumulator outlet pipe is connect with regeneration gas cooler inlet pipe, and the regeneration gas cooler outlet pipe passes through valve
Door is connect with the raw natural gas pipe, and the circularly-supercharged machine import setting purified gas supplements pipeline.
2. a kind of process system for removing carbon dioxide in natural according to claim 1, it is characterized in that: the suction
Attached tower A, the adsorption tower B, the adsorption tower C filler are molecular sieve, molecular sieve and active carbon multiple-hearth, molecular sieve and silicon
Glue multiple-hearth or molecular sieve are combined with activated alumina.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820991189.9U CN208829616U (en) | 2018-06-26 | 2018-06-26 | Remove the process system of carbon dioxide in natural |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820991189.9U CN208829616U (en) | 2018-06-26 | 2018-06-26 | Remove the process system of carbon dioxide in natural |
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| Publication Number | Publication Date |
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| CN208829616U true CN208829616U (en) | 2019-05-07 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108641765A (en) * | 2018-06-26 | 2018-10-12 | 兰文旭 | Remove the process system and method for carbon dioxide in natural |
| CN110408446A (en) * | 2019-08-01 | 2019-11-05 | 兰文旭 | The liquefied natural gas pre-processing device and method that UF membrane is combined with temp.-changing adsorption |
-
2018
- 2018-06-26 CN CN201820991189.9U patent/CN208829616U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108641765A (en) * | 2018-06-26 | 2018-10-12 | 兰文旭 | Remove the process system and method for carbon dioxide in natural |
| CN110408446A (en) * | 2019-08-01 | 2019-11-05 | 兰文旭 | The liquefied natural gas pre-processing device and method that UF membrane is combined with temp.-changing adsorption |
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Granted publication date: 20190507 Termination date: 20210626 |