CN104848654A - Method and device for extracting argon from natural gas - Google Patents
Method and device for extracting argon from natural gas Download PDFInfo
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- CN104848654A CN104848654A CN201510310285.3A CN201510310285A CN104848654A CN 104848654 A CN104848654 A CN 104848654A CN 201510310285 A CN201510310285 A CN 201510310285A CN 104848654 A CN104848654 A CN 104848654A
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Abstract
The invention provides a device for extracting argon from natural gas, comprising feed gas compressor, a pre-cooling system, a purification system and a main heat exchanger which are connected by pipelines. The device provided by the invention is characterized by further comprising a helium separation tower, a helium separation tower reboiler, a nitrogen removing tower, a methane removing tower, an argon refining tower, a sub-cooler and pipelines and valves which connect the above components. The invention provides a method for extracting argon by taking the natural gas as a raw material at the same time, and the acquired argon is high in degree of purity and free of radiation. Meanwhile, the method and the device provided by the invention adopt a process of full distillation, the continuous operating time is long, and the equipment is stable.
Description
Technical field
The present invention relates to gas component to be separated, more particularly the present invention relates to a kind of Full distillation that utilizes from natural gas and extract the separation method of argon gas and corresponding device.
Background technology
The aerial content of argon gas is 0.93%, and helium is 5.2ppm.Helium in atmosphere content very little, normally extracts from natural gas.And in atmosphere, argon content ranking the 3rd, rich content, it is convenient to extract, and all adopts air to be raw material so argon gas extracts.Present more than 10,000 large empty dividing were typically equipped with Full distillation Argon recovery subsystem.Common flow process is: air is compressed to required pressure through air compressor machine, removes carbon dioxide, water and hydrocarbon partial through precooling purifying.Be divided into two parts before entering ice chest, a part enters turbo-expander end and is pressurized to 0.65 ~ 0.8MPa, is then cooled to 20 DEG C through cooler, enters after main heat exchanger is cooled to-120 DEG C ~-140 DEG C, enter expander to slightly higher than upper tower pressure, enter Shang Ta.Another part air is through main heat exchanger and the gas that backflowed is cooled to liquefaction, start to be separated after entering lower tower, the air entering lower tower bottom passes column plate and carries out caloic exchange with the phegma on column plate, such result is, obtain pure nitrogen gas on Xia Ta top, obtain oxygen-enriched liquid air at tower Fu.Lower top of tower overwhelming majority nitrogen enters the condensation side of condenser/evaporator, and nitrogen is by releasing heat the evaporation of the liquid oxygen of upper tower bottom there, self obtains condensation and as lower tower phegma.Part liquid nitrogen is also had after the mistake of subcooler is cold, to be sent to upper top of tower, the phegma of top of tower on work.Excessively cold through subcooler of the oxygen-enriched liquid air extracted out from the tower Fu of lower tower, enters tower top as upper tower phegma after throttling.Oxygen product finally produces in upper tower rectifying, extracts oxygen out and enters main heat exchanger, go out device and send as gas product after oxygen re-heat from upper tower bottom.Pure nitrogen gas is extracted out from upper top of tower, first in subcooler by pure liquid nitrogen and oxygen-enriched liquid air re-heat, then enter in main heat exchanger and go out device after re-heat.Draw dirty nitrogen from upper tower top, through subcooler, main heat exchanger re-heat to 21 DEG C cooling box, then enter electric heater as regenerating molecular sieve gas, excessive gas emptying.In the middle part of upper tower, extract a certain amount of argon fraction send into crude argon column, crude argon column is structurally divided into two sections, and the phegma bottom second segment argon column sends into first paragraph top as phegma through liquor pump, obtains purity and is about 98.5%Ar, 2ppm O through crude argon column rectifying
2crude argon, send in the middle part of pure argon column through liquefier post liquefaction, bottom pure argon column, obtain seminal fluid argon through pure argon column rectifying.The advantage of the method is argon abundant raw material, and extraction cost is low.But although argon content is enriched in air, argon also has multiple isotope, stable coordination have argon-40 (
40ar) natural content 99.6%, argon-36 (
36ar) natural content 0.34% and argon-38 (
38ar) natural content 0.06%.And the argon-39 of the instability to generate via cosmic-ray bombardment argon-40 (
39ar), so, be limited to the argon gas impact in air, its argon isotope cannot be separated, its radiation can affect the requirement of the special occasions such as laboratory to argon gas, especially, now during a lot of laboratory situations requirement several part per billion impurity content, air is that the argon gas of raw material obviously can not meet its requirement.
Summary of the invention
The object of the invention is each component feature of absence for prior art and natural gas, provide a kind of from natural gas Full distillation extract the method and apparatus of argon gas, ensure extracting method and stable equipment operation, efficient simultaneously.
The present invention solves the problems of the technologies described above adopted technical scheme:
Extract a method for argon gas in natural gas, comprise the following steps:
Step 1: by natural gas after being compressed to required pressure in feed gas compressor after chilldown system precooling and purification system purifying, in main heat exchanger, cooling also, after helium knockout tower reboiler is condensed into liquid, enters helium knockout tower;
Step 2: the liquid obtained bottom helium knockout tower enters nitrogen-rejection column after choke valve step-down, most of the nitrogen component escapes and enter nitrogen circulating system from nitrogen-rejection column top becomes circulating nitrogen gas, the mixed liquor of methane and argon gas and trace nitrogen component are extracted out and are entered except methane tower bottom nitrogen-rejection column, methane enters subcooler recovery cold from extracting out in liquid form except methane tower bottom, a small amount of nitrogen is contained from except methane top of tower crude argon out, enter pure argon column, trace nitrogen gas Component seperation, bottom pure argon column, obtain satisfactory straight argon liquid.
For optimizing above-mentioned extracting method, the concrete measure taked also comprises:
Above-mentioned circulating nitrogen gas in step 1 through nitrogen circulation compressor compresses laggard enter main heat exchanger cooling, then enter nitrogen-rejection column reboiler, except methane tower reboiler, pure argon column reboiler, for the nitrogen-rejection column of correspondence, provide heat except methane tower, pure argon column.
In step 1 from nitrogen-rejection column reboiler, except after methane tower reboiler, pure argon column reboiler liquid nitrogen out converge, a part enters liquid nitrogen gas-liquid separator after subcooler cools throttling again, bottom above-mentioned liquid nitrogen gas-liquid separator liquid nitrogen out as low-temperature receiver enter helium knockout tower condenser/evaporator, nitrogen-rejection column condenser/evaporator. except methane tower condenser/evaporator and pure argon column condenser/evaporator, for rectifying provides liquid.
From the part nitrogen that heat exchanger is come in, from heat exchanger out after enter decompressor, this part nitrogen after expansion and the nitrogen after four corresponding condenser/evaporators gasify, liquid nitrogen gas-liquid separator top nitrogen out and enter after subcooler reclaims cold together from corresponding reboiler part nitrogen out, final and nitrogen-rejection column top nitrogen out merges into one, enters nitrogen circulation compressor and participate in circulation after entering main heat exchanger re-heat.
The present invention also provides the device extracting argon gas in a kind of natural gas, include feed gas compressor, chilldown system, purification system and main heat exchanger that pipeline connects, it is characterized in that, said apparatus also include helium knockout tower, helium knockout tower reboiler, nitrogen-rejection column, except methane tower, pure argon column, subcooler and pipeline, valve that above-mentioned parts are connected, natural gas is successively through feed gas compressor, after chilldown system and purification system, cooling in main heat exchanger also enters helium knockout tower after helium knockout tower reboiler is condensed into liquid, the liquid obtained bottom helium knockout tower enters nitrogen-rejection column after choke valve step-down, the mixed liquor of methane and argon gas and trace nitrogen component are extracted out and are entered except methane tower bottom nitrogen-rejection column, methane enters subcooler recovery cold from extracting out in liquid form except methane tower bottom, a small amount of nitrogen is contained from except methane top of tower crude argon out, enter pure argon column and obtain satisfactory straight argon liquid.
In order to optimize said apparatus further, the concrete measure taked also comprises:
Said apparatus also has nitrogen circulation compressor, above-mentioned helium knockout tower, nitrogen-rejection column, except methane tower, pure argon column correspondingly arrange and be connected with helium knockout tower reboiler, helium knockout tower condenser/evaporator, nitrogen-rejection column reboiler, nitrogen-rejection column condenser/evaporator, except methane tower reboiler, except methane tower condenser/evaporator, pure argon column reboiler, pure argon column condenser/evaporator.
Above-mentioned subcooler is also connected with liquid nitrogen gas-liquid separator.
Above-mentioned device also includes the decompressor be connected with subcooler with above-mentioned heat exchanger.
Apply method and apparatus of the present invention and to carry out in natural gas argon gas when extracting, first by natural gas entering fractionating column ice chest after being compressed to required pressure in compressor after chilldown system, purification system purifying.Then, cool in main heat exchanger again after the reboiler at the bottom of helium knockout tower is condensed into liquid, enter helium knockout tower.Be separated tower top from helium and obtain the emptying after main heat exchanger re-heat of raw helium gas.Bottom helium knockout tower, liquid out enters nitrogen-rejection column after choke valve step-down.Most of the nitrogen component is discharged from nitrogen-rejection column top, enters nitrogen circulating system.The mixed liquor of methane and argon gas and trace nitrogen component are extracted out and are entered except methane tower bottom nitrogen-rejection column, and methane enters subcooler recovery cold, main heat exchanger re-heat from extracting out in liquid form except methane tower bottom, gives user or its use.Finally, contain a small amount of nitrogen from except methane top of tower crude argon out, enter pure argon column, trace nitrogen gas Component seperation, bottom pure argon column, obtain satisfactory straight argon liquid.
Circulating nitrogen gas through nitrogen compressor compression laggard enter main heat exchanger cooling, then enter nitrogen-rejection column reboiler, except methane tower reboiler, pure argon column reboiler, for the nitrogen-rejection column of correspondence, provide heat except methane tower, pure argon column.After converging from three tower reboilers liquid nitrogen out, some enters liquid nitrogen gas-liquid separator after subcooler cools throttling again, bottom gas-liquid separator, liquid nitrogen out enters the condenser/evaporator of four rectifying columns as low-temperature receiver, for rectifying provides liquid.From another strand of nitrogen that heat exchanger is come in, from heat exchanger out after enter decompressor, expand after nitrogen enter subcooler reclaim cold.Nitrogen after gasifying with condenser/evaporator again, liquid nitrogen gas-liquid separator top nitrogen out and enter after subcooler reclaims cold from the nitrogen of reboiler part out, one is merged into nitrogen-rejection column top nitrogen out, enter nitrogen pressure contracting after entering main heat exchanger re-heat and participate in circulation, if any unnecessary nitrogen, in this emptying.
Compared with prior art, the present invention is that raw material extracts argon gas with natural gas, and the divided gas flow purity obtained is high, radiationless, and method and apparatus of the present invention uses Full distillation technique simultaneously, and continuous operating time is long, and equipment is stablized.
Accompanying drawing explanation
Fig. 1 is schematic flow sheet of the present invention.
Detailed description of the invention
In order to make the object, technical solutions and advantages of the present invention clearly, below with reference to accompanying drawing, technical scheme of the present invention is further elaborated.
Fig. 1 is schematic flow sheet of the present invention.
Reference numeral is wherein: feed gas compressor 1; Chilldown system 2; Purification system 3; Main heat exchanger 4; Helium knockout tower 5; Helium knockout tower reboiler 6; Nitrogen-rejection column 7; Nitrogen-rejection column reboiler 8; Except methane tower 9; Except methane tower reboiler 10; Pure argon column 11; Pure argon column reboiler 12; Helium knockout tower condenser/evaporator 13; Nitrogen-rejection column condenser/evaporator 14; Except methane tower condenser/evaporator 15; Pure argon column condenser/evaporator 16; Liquid nitrogen gas-liquid separator 17; Subcooler 18; Decompressor 22; Nitrogen circulation compressor 23; Vavuum pump 24.
Carry out detailed and concrete introduction below by specific embodiment to the present invention, to make better to understand the present invention, but following embodiment does not limit the scope of the invention.
Embodiment 1
Feed gas composition: helium 1.58%; Argon gas: 0.27%; Nitrogen: 81.91%; Methane: 16.23%; Other are water and carbon dioxide; Flow is: 700Nm
3/ h
Unstripped gas after being compressed to the required pressure of 4.0MPa (G) in feed gas compressor 1 after chilldown system 2 cools to 10 DEG C, purification system 3 purifying enters fractionating column ice chest after removing water (dew point <-65 DEG C and carbon dioxide content <1ppm of water).In main heat exchanger 4, be cooled to-135 DEG C again after helium knockout tower reboiler 6 is condensed into liquid (because helium is difficult to liquefaction, actual liquefaction rate is 83%), enter helium knockout tower 5.Helium knockout tower number of theoretical plate 10 pieces, obtains raw helium gas (helium purity is 65.82%) from helium knockout tower 5 top after main heat exchanger 4 re-heat is to 17 DEG C, goes out tower supply user.
Bottom helium knockout tower 5, liquid is out depressurized to after 0.15MPa (G) through choke valve and enters nitrogen-rejection column 7.The theoretical cam curve of nitrogen-rejection column 7 is 60 pieces, and most of the nitrogen component is discharged from nitrogen-rejection column 7 top, and the nitrogen amount of discharge is 608Nm
3/ h, nitrogen gas purity is: 99.997%, enters nitrogen circulating system.The mixed liquor of methane and argon gas and trace nitrogen component are extracted out and are entered except methane tower 9 bottom nitrogen-rejection column 7, and methane enters subcooler 18 reclaim cold, main heat exchanger 4 re-heat from except extracting out in liquid form bottom methane tower 9, and give user or its use, methane content is 121Nm
3/ h.From except methane tower 9 top crude argon out contains a small amount of nitrogen, (component is: argon gas: 99.938%; Nitrogen: 0.0615%), enters pure argon column 11, trace nitrogen gas Component seperation, bottom pure argon column 11, obtains satisfactory straight argon liquid.
Cyclic nitrogen tolerance is 4000Nm
3/ h through nitrogen compressor compress 23 laggard enter main heat exchanger 4 cool to-120 DEG C, then enter nitrogen-rejection column reboiler 8 (2757Nm
3/ h), except methane tower reboiler 10 (160Nm
3/ h), pure argon column reboiler 12 (20Nm
3/ h), for the nitrogen-rejection column 7 of correspondence, provide heat except methane tower 9, pure argon column 11.Some (2010Nm after converging from three tower reboilers liquid nitrogen out
3/ h) through subcooler 18 cool-153.6 DEG C be throttled to 0.04MPa (G) again after enter liquid nitrogen gas-liquid separator 17, bottom gas-liquid separator 17, amount of liquid nitrogen is out 947.2Nm
3/ h, enters the condenser/evaporator (13,14,15,16) of four rectifying columns, for rectifying provides liquid as low-temperature receiver.From another gang of nitrogen (1060Nm that heat exchanger 4 is come in
3/ h), from heat exchanger out after enter decompressor 22, expand into-171.8 DEG C, 0.4MPa (G), after expanding, nitrogen enters subcooler 18 and reclaims cold.With the nitrogen after condenser/evaporator gasifies, liquid nitrogen gas-liquid separator 17 top nitrogen out and from the nitrogen of reboiler part out enter subcooler reclaim cold after re-heat to-155.9 DEG C, one is merged into nitrogen-rejection column 7 top nitrogen out, enter main heat exchanger 4 re-heat and enter nitrogen pressure contracting participation circulation after 17 DEG C, if any unnecessary nitrogen, in this emptying.
The present invention is that raw material extracts argon gas with natural gas, and the divided gas flow purity obtained is high, radiationless, and method and apparatus of the present invention uses Full distillation technique simultaneously, and continuous operating time is long, and equipment is stablized.
Be described in detail specific embodiments of the invention above, but it is just as example, the present invention is not restricted to specific embodiment described above.To those skilled in the art, any equivalent modifications that the present invention is carried out and substituting also all among category of the present invention.Therefore, equalization conversion done without departing from the spirit and scope of the invention and amendment, all should contain within the scope of the invention.
Claims (8)
1. extract a method for argon gas in natural gas, it is characterized in that, comprise the following steps:
Step 1: by natural gas after being compressed to required pressure in feed gas compressor (1) after chilldown system (2) precooling and purification system (3) purifying, cooling in main heat exchanger (4) also, after helium knockout tower reboiler (6) is condensed into liquid, enters helium knockout tower (5);
Step 2: the liquid obtained in helium knockout tower (5) bottom enters nitrogen-rejection column (7) after choke valve step-down, from nitrogen-rejection column (7), top escapes and enter nitrogen circulating system to most of the nitrogen component becomes circulating nitrogen gas, the mixed liquor of methane and argon gas and trace nitrogen component are extracted out from nitrogen-rejection column (7) bottom and are entered except methane tower (9), methane enters subcooler (18) recovery cold from extracting out in liquid form except methane tower (9) bottom, a small amount of nitrogen is contained from except methane tower (9) top crude argon out, enter pure argon column (11), trace nitrogen gas Component seperation, satisfactory straight argon liquid is obtained from pure argon column (11) bottom.
2. in a kind of natural gas according to claim 1, extract the method for argon gas, it is characterized in that, described circulating nitrogen gas in step 1 through nitrogen circulation compressor (23) compress laggard enter main heat exchanger (4) cooling, enter nitrogen-rejection column reboiler (8) again, except methane tower reboiler (10), pure argon column reboiler (12), for the nitrogen-rejection column (7) of correspondence, provide heat except methane tower (9), pure argon column (11).
3. in a kind of natural gas according to claim 2, extract the method for argon gas, it is characterized in that, from nitrogen-rejection column reboiler (8) in step 1, except methane tower reboiler (10), after pure argon column reboiler (12) liquid nitrogen out converges, a part enters liquid nitrogen gas-liquid separator (17) after subcooler (18) cools throttling again, helium knockout tower condenser/evaporator (13) is entered as low-temperature receiver from described liquid nitrogen gas-liquid separator (17) bottom liquid nitrogen out, nitrogen-rejection column condenser/evaporator (14), . except methane tower condenser/evaporator (15) and pure argon column condenser/evaporator (16), for rectifying provides liquid.
4. in a kind of natural gas according to claim 2, extract the method for argon gas, it is characterized in that, from the part nitrogen that heat exchanger (4) is come in, from heat exchanger (4) out after enter decompressor (22), this part nitrogen after expansion at four corresponding condenser/evaporators (13, 14, 15, 16) nitrogen after gasification, liquid nitrogen gas-liquid separator (17) top nitrogen out and enter after subcooler (18) reclaims cold together from corresponding reboiler part nitrogen out, final and nitrogen-rejection column (7) top nitrogen out merges into one, enter nitrogen circulation compressor (23) after entering main heat exchanger (4) re-heat and participate in circulation.
5. in a natural gas, extract the device of argon gas, include feed gas compressor (1), chilldown system (2), purification system (3) and main heat exchanger (4) that pipeline connects, it is characterized in that, described device also include helium knockout tower (5), helium knockout tower reboiler (6), nitrogen-rejection column (7), except methane tower (9), pure argon column (11), subcooler (18) and pipeline, valve that above-mentioned parts are connected, natural gas is successively through feed gas compressor (1), after chilldown system (2) and purification system (3), cooling in main heat exchanger (4) also enters helium knockout tower (5) after helium knockout tower reboiler (6) is condensed into liquid, the liquid obtained in helium knockout tower (5) bottom enters nitrogen-rejection column (7) after choke valve step-down, the mixed liquor of methane and argon gas and trace nitrogen component are extracted out from nitrogen-rejection column (7) bottom and are entered except methane tower (9), methane enters subcooler (18) recovery cold from extracting out in liquid form except methane tower (9) bottom, a small amount of nitrogen is contained from except methane tower (9) top crude argon out, enter pure argon column (11) and obtain satisfactory straight argon liquid.
6. in a kind of natural gas according to claim 5, extract the device of argon gas, it is characterized in that, described device also has nitrogen circulation compressor (23), described helium knockout tower (5), nitrogen-rejection column (7), except methane tower (9), pure argon column (11) correspondingly arranges and is connected with helium knockout tower reboiler (6), helium knockout tower condenser/evaporator (13), nitrogen-rejection column reboiler (8), nitrogen-rejection column condenser/evaporator (14), except methane tower reboiler (10), except methane tower condenser/evaporator (15), pure argon column reboiler (12), pure argon column condenser/evaporator (16).
7. extract the device of argon gas in a kind of natural gas according to claim 5, it is characterized in that, described subcooler (18) is also connected with liquid nitrogen gas-liquid separator (17).
8. extract the device of argon gas in a kind of natural gas according to claim 5, it is characterized in that, also include the decompressor (22) be connected with subcooler (18) with described heat exchanger (4).
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| CN109734064A (en) * | 2019-01-03 | 2019-05-10 | 北京中科富海低温科技有限公司 | A kind of helium production system and production method |
| CN110542279A (en) * | 2019-09-10 | 2019-12-06 | 苏州市兴鲁空分设备科技发展有限公司 | argon tail gas recovery and purification device containing methane and hydrocarbon |
| CN110608582A (en) * | 2019-09-10 | 2019-12-24 | 苏州市兴鲁空分设备科技发展有限公司 | Argon tail gas recycling and purifying device |
| CN114777420A (en) * | 2022-03-31 | 2022-07-22 | 中科瑞奥能源科技股份有限公司 | System and method for recovering argon and high-purity methane in hydrogen system |
| CN115371359A (en) * | 2022-08-25 | 2022-11-22 | 北京航天试验技术研究所 | Sabatier device reaction gas separation and liquefaction system and method applied to Mars surface |
| CN116987536A (en) * | 2023-06-15 | 2023-11-03 | 英德市西洲气体有限公司 | Argon removal process for methane tower |
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| CN114777420A (en) * | 2022-03-31 | 2022-07-22 | 中科瑞奥能源科技股份有限公司 | System and method for recovering argon and high-purity methane in hydrogen system |
| CN115371359A (en) * | 2022-08-25 | 2022-11-22 | 北京航天试验技术研究所 | Sabatier device reaction gas separation and liquefaction system and method applied to Mars surface |
| CN116987536A (en) * | 2023-06-15 | 2023-11-03 | 英德市西洲气体有限公司 | Argon removal process for methane tower |
| CN116987536B (en) * | 2023-06-15 | 2024-03-08 | 英德市西洲气体有限公司 | Argon removal process for methane tower |
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