CN209307312U - A kind of separator of hydrocarbon in separable natural gas - Google Patents
A kind of separator of hydrocarbon in separable natural gas Download PDFInfo
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- CN209307312U CN209307312U CN201822244930.8U CN201822244930U CN209307312U CN 209307312 U CN209307312 U CN 209307312U CN 201822244930 U CN201822244930 U CN 201822244930U CN 209307312 U CN209307312 U CN 209307312U
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Abstract
The utility model belongs to natural gas processing technical field, more particularly to a kind of separator of the hydrocarbon in separable natural gas, including tower body, packing layer, packing support device, liquid spraying device and activated carbon treatment device, described filler layer is composed of whole rule filler and dumped packing, the packing support device is fixed in tower body, described filler layer is deposited on packing support device, the top of packing layer is arranged in the liquid spraying device, and the activated carbon treatment device is arranged in tower body inner tip.Packing layer in the utility model is composed of whole rule filler and dumped packing, gas, liquid can be made to be evenly distributed the two combination, to improve de- hydrocarbon efficiency, while be reduced cost；Liquid can be effectively equably sprayed onto filler by spray equipment, avoid that channeling occurs；Activated carbon treatment device further absorbs the heavy hydrocarbon in natural gas, guarantees the de- hydrocarbon rate in natural gas processing.
Description
Technical field
The utility model belongs to natural gas processing technical field, and in particular to a kind of separation of the hydrocarbon in separable natural gas
Device.
Background technique
Natural gas can generate retrograde condensation phenomenon because of the variation of temperature or pressure, here it is hydrocarbonaceous bands during collecting defeated
The influence come, the especially hydrocarbonaceous of liquid can cause corrosion and blocking to pipeline collection is defeated.Through to natural gas on-site sample examination,
For heavy hydrocarbons content in 6.2%-8.5%, specific gravity is larger, if these heavy hydrocarbon components do not remove, is existed using the automobile of the class natural gas
It is easy that liquid hydrocarbon is precipitated in use process, to the problems such as blocking fuel gas pipeline occur；But meanwhile these heavy hydrocarbons are to change well
Work raw material can be processed into the high product of added value, it will bring to enterprise if can be separated by technological means
Great economic benefit.
Traditional natural qi exhaustion hydrocarbon technology mainly uses liquid dissolution method, and liquid dissolution method generally uses packed tower to be inhaled
It receives, traditional packed tower all cannot play the efficiency of packed tower as packing layer using single filler well in this way, and through filling out
Treated in material, and unstripped gas is likely present certain heavy hydrocarbon, and traditional packed tower uses single processing mode treatment effect
It is limited.
Utility model content
In order to solve the above problems existing in the present technology, the utility model aim is to provide a kind of separable natural gas
In hydrocarbon separator, natural gas is handled simultaneously using liquid dissolution method and active carbon adsorption, improves de- hydrocarbon effect
Fruit.
The technology employed by the present utility model is a kind of separator of the hydrocarbon in separable natural gas, including tower
Body, packing layer, packing support device, liquid spraying device and activated carbon treatment device, described filler layer by whole rule filler and
Dumped packing is composed, and the packing support device is fixed in tower body, and described filler layer is deposited on packing support device,
The top of packing layer is arranged in the liquid spraying device, and the activated carbon treatment device is arranged in tower body inner tip.
Further, the activated carbon treatment device includes: active carbon layer, regeneration gas air inlet pipe and regeneration gas escape pipe,
The active carbon layer is fixedly connected on tower body top, and the regeneration gas air inlet pipe is arranged below active carbon layer, the regeneration gas
Escape pipe is arranged above active carbon layer, is provided with valve on the regeneration gas air inlet pipe and regeneration gas escape pipe.Unstripped gas
By packing layer and with after the liquid reactions in packing layer, major part heavy hydrocarbon therein has been absorbed, but may be still
The heavy hydrocarbon of portion of residual is additionally provided with active carbon layer to guarantee de- hydrocarbon rate above packing layer, and active carbon layer is used for into one
Step absorbs the heavy hydrocarbon in unstripped gas, since the absorption number of active carbon layer is limited, in order to guarantee the absorbability of active carbon layer,
The upper and lower of active carbon layer is respectively arranged with regeneration gas air inlet pipe and regeneration gas escape pipe, for importing regeneration gas, to active carbon
Layer is regenerated, and guarantees the absorbability of active carbon layer.
Further, the liquid spraying device includes liquid feed pipe, liquid distribution trough and branching block, the liquid point
Cloth device is fixed in tower body, and multiple branching blocks are provided on the liquid distribution trough, are evenly arranged on the branching block multiple
Aperture, the liquid distribution trough are connected to liquid feed pipe.The quality that liquid initial is distributed in packing layer not only affects filler
Mass-transfer efficiency, but also the operating flexibility of filler can be had an impact, therefore in order to reduce since the bad distribution of liquid is drawn
The enlarge-effect risen, gives full play to the efficiency of filler, is provided with liquid distribution trough, liquid distribution trough mainly equably sprays liquid
It is spread across in packing layer, is connected on liquid distribution trough with liquid feed pipe, liquid feed pipe is used to liquid importeding into liquid distribution
In device, valve is provided on liquid feed pipe, for controlling the liquid inlet of liquid feed pipe, in order to further increase liquid
The uniformity of body sprinkling, branching block is additionally provided on liquid distribution trough, multiple apertures are evenly arranged on the branching block, point
Liquid is distributed to different zones above packing layer by stream block, and the aperture being uniformly arranged on branching block sprays liquid in spraying form
It is spread across on packing layer, maximumlly to improve the uniformity of liquid sprinkling.
Further, Liquid extracting pump, the tower body outer wall are provided between the liquid feed pipe and liquid distribution trough
It is provided with support frame, the Liquid extracting pump fixed setting is on the support frame.Liquid extracting pump is for by Liquid extracting to liquid
In distributor, support frame is used to support Liquid extracting pump, is disposed at outside tower body and is easily installed and overhauls.
Further, described filler layer is made of the whole rule filler on upper layer and the dumped packing of lower layer, the dumped packing
Thickness be thicker than it is whole rule filler thickness.Filler is one of core component of the present apparatus, is the mass transfer of gas-liquid two-phase contact, and can
To have and strengthen gas turbulence, reduce the effect of resistance of gas mass transfer, have to the working performance of the present apparatus as heat exchange surface
Tremendous influence.Structured packing is by many filler monomer compositions with same geometry, they are in a manner of whole block
Be seated in tower, have the advantages that increase gap flow phenomenon rate and effective contact surface area, strengthen two-phase empir-ical formulation and
Reduce wall stream and ditch, if using single structured packing, it is not only with high costs, but also limited by flow parameter larger；It dissipates
Filling material is also known as dumped packing, has easily fabricated, cheap feature, but only it is single using dumped packing when, liquid
The case where body is unevenly distributed on filling surface, and there are wall streams, channel, but also that there are specific surface areas is smaller, voidage is small
Problem.The advantages of forming packing layer, can keep two kinds of fillers simultaneously the mode that whole rule filler, dumped packing are combined, makes
Disadvantage is complementary, effectively changes the distribution of gas phase and liquid phase, increasing specific surface area and voidage, improves de- hydrocarbon efficiency, and control
Cost.Structured packing has ripple packing, lattices filler and Impulse packing etc., this place uses Corrugated Structured Packings；It is in bulk to fill out
Material has Raschig ring filler, Pall ring filler, saddle class filler, net form filler, cross ring filler etc., this place is filled out using Pall ring
Material.
Further, the tower body bottom is provided with air inlet pipe, and gas point is provided between the air inlet pipe and packing layer
Cloth apparatus is provided with liquid re-distributor between described filler layer.After unstripped gas enters tower body out of air inlet pipe, it is unevenly distributed
Even, the contact with packing layer is also insufficient, and in order to improve this status, gas distribution is provided between air inlet pipe and packing layer
Device improves contact uniformity of the unstripped gas with packing layer.And if filler layer depth is blocked up, liquid is easy shape in packing layer
Wall-forming flow phenomenon causes liquid distribution uneven, influences de- hydrocarbon efficiency, in order to avoid this case, two described filler layers it
Between be provided with liquid re-distributor, liquid can be equably sprayed onto packing layer by liquid re-distributor, improve liquid flow direction
The distributing homogeneity when filler of bottom end.
Further, vortex-flow and defrosting device is provided with above the activated carbon treatment device, the vortex-flow and defrosting device is solid
Surely it is connected in tower body inner wall.Since gas is when tower top leaves packed tower, a large amount of liquid foam and droplet may be had, to return
This Partial Liquid Phase is received, vortex-flow and defrosting device is provided with above the activated carbon treatment device, vortex-flow and defrosting device is by several pieces of fixations
Eddy flow plate composition, when gas passes through, generate rotary motion, cause a centrifugal force field, drop under the action of the centrifugal force, to
Tower wall movement realizes gas-liquid separation.
Further, the bottom of the tower body is provided with liquid reserve tank, and the liquid reserve tank is externally connected with acid-proof pump.Work as liquid flow
It crosses whole packing layers and with after raw material solid/liquid/gas reactions, a large amount of heavy hydrocarbon is contained in liquid, needs for this partially liq to be collected into together
And handled, therefore be fixedly installed liquid reserve tank in the bottom of tower body, the liquid for flowing to bottom can be pooled to by liquid reserve tank
Together, the liquid with heavy hydrocarbon is discharged in corresponding processing unit by the acid-proof pump being arranged in outside liquid reserve tank.
Further, filler compacting device is provided on the whole rule filler of the top layer of described filler layer.Filler compresses dress
It sets and is mounted on packing layer upper end, be the bed for keeping packing layer fixed for a height, to keep uniform gap
Structure keeps operation normal, stable, prevents when high pressure drop, instantaneous load fluctuation, and packing layer generation loosens or bounce,
Guarantee the de- hydrocarbon efficiency of the present apparatus.
Further, it is provided with manhole on the side wall of the tower body and sees inspection window.Manhole facilitates maintenance personal to enter tower body
It is inside overhauled, sees the case where inspection window is convenient in observing tower body.
The utility model has the following beneficial effects:
By setting packing layer, liquid spraying device and activated carbon treatment device, packing layer is by whole rule filler and in bulk fills out
Material is composed, and whole rule filler has the advantages that increase gap flow phenomenon rate and effective contact surface area, strengthens the transverse direction of two-phase
Mixing and reduce wall stream and ditch, dumped packing has easily fabricated, cheap feature, by the two combination can make gas,
Liquid is evenly distributed, and improves the distribution of gas, liquid to improve de- hydrocarbon efficiency, while reducing cost；Spray equipment can effectively by
Liquid is equably sprayed onto filler, avoids that channeling occurs；In the further separating natural gas of activated carbon treatment device energy
Heavy hydrocarbon, guarantee natural gas processing in de- hydrocarbon rate.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
In figure: 1- tower body；2- air inlet pipe；3- packing support device；The whole rule filler of 4-；5- dumped packing；6- filler compresses
Device；7- liquid re-distributor；8- liquid distribution trough；9- branching block；10- support frame；11- liquid feed pipe；12- Liquid extracting
Pump；13- gas tip；14- regeneration gas air inlet pipe；15- active carbon layer；16- sees inspection window；17- vortex-flow and defrosting device；18- valve；
19- regeneration gas escape pipe；20- escape pipe；21- manhole；22- distribution device in gas-fluid；23- liquid reserve tank；24- acid-proof pump；25- sled
Seat.
Specific embodiment
With reference to the accompanying drawing and specific embodiment is further elaborated the utility model.
Embodiment 1:
As shown in Figure 1, a kind of separator of the hydrocarbon in separable natural gas, including tower body 1, packing layer, packing support
Device 3, liquid spraying device and activated carbon treatment device, described filler layer by whole rule filler 4 and dumped packing 5 combination and
At the packing support device 3 is fixed in tower body 1, and described filler layer is deposited on packing support device 3, the liquid spray
The top of packing layer is arranged in shower device, and the activated carbon treatment device is arranged in 1 inner tip of tower body.
The utility model is filled out by setting packing layer, liquid spraying device and activated carbon treatment device, packing layer by whole rule
Material 4 and dumped packing 5 are composed, and whole rule filler 4 has the advantages that increase gap flow phenomenon rate and effective contact surface area, by force
Change the empir-ical formulation of two-phase and reduce wall stream and ditch, dumped packing 5 has easily fabricated, cheap feature, by the two
In conjunction with that air-liquid can be made to be evenly distributed, improve the distribution of gas, liquid to improve de- hydrocarbon efficiency, while reducing cost；Spray dress
Setting effectively equably to be sprayed onto liquid in filler, avoid that channeling occurs；Activated carbon treatment device can be further
Heavy hydrocarbon in separating natural gas guarantees the de- hydrocarbon rate in natural gas processing.
Embodiment 2:
As the optimal technical scheme of the utility model, on the basis of embodiment 1, the activated carbon treatment device packet
Include: active carbon layer 15, regeneration gas air inlet pipe 14 and regeneration gas escape pipe 19, the active carbon layer 15 are fixedly connected on tower body 1
Portion, the regeneration gas air inlet pipe 14 are arranged below active carbon layer 15, and the regeneration gas escape pipe 19 is arranged in active carbon layer 15
Top is provided with valve 18 on the regeneration gas air inlet pipe 14 and regeneration gas escape pipe 19.Unstripped gas by packing layer and with
After liquid reactions in packing layer, major part heavy hydrocarbon therein has been absorbed, but possible or portion of residual heavy hydrocarbon,
In order to guarantee de- hydrocarbon rate, active carbon layer 15 is additionally provided with above packing layer, active carbon layer 15 is for further absorbing raw material
Heavy hydrocarbon in gas, since the absorption number of active carbon layer 15 is limited, in order to guarantee the absorbability of active carbon layer 15, in active carbon
The upper and lower of layer 15 is respectively arranged with regeneration gas air inlet pipe 14 and regeneration gas escape pipe 19, for importing regeneration gas, to active carbon
Layer 15 is regenerated, and guarantees the absorbability of active carbon layer 15.
Embodiment 3:
As the optimal technical scheme of the utility model, on the basis of embodiment 1, the liquid spraying device includes liquid
Body feed pipe 11, liquid distribution trough 8 and branching block 9, the liquid distribution trough 8 are fixed in tower body 1, the liquid distribution trough 8
On be provided with multiple branching blocks 9, multiple apertures, the liquid distribution trough 8 and liquid feedstock are evenly arranged on the branching block 9
Pipe 11 is connected to.The quality that liquid initial is distributed in packing layer not only affects the mass-transfer efficiency of filler, but also can be to filler
Operating flexibility has an impact, therefore in order to reduce the enlarge-effect due to caused by liquid bad distribution, gives full play to filler
Efficiency is provided with liquid distribution trough 8, and liquid is mainly equably sprayed onto packing layer by liquid distribution trough 8, liquid distribution trough 8
Upper to be connected to liquid feed pipe 11, liquid feed pipe 11 is for liquid to be imported into liquid distribution trough 8, in liquid feed pipe 11
On be provided with valve 18, for controlling the liquid inlet of liquid feed pipe 11, in order to further increase liquid sprinkling it is uniform
Degree, is additionally provided with branching block 9 on liquid distribution trough 8, is evenly arranged with multiple apertures on the branching block 9, and branching block 9 is by liquid
Body is distributed to different zones above packing layer, and the aperture being uniformly arranged on branching block 9 is sprayed the liquid into spraying form to be filled out
On the bed of material, maximumlly to improve the uniformity of liquid sprinkling.
Liquid extracting pump 12,1 outer wall of the tower body setting are provided between the liquid feed pipe 11 and liquid distribution trough 8
There is support frame 10, the Liquid extracting pump 12 is fixed on support frame 10.Liquid extracting pump 12 is for arriving Liquid extracting
In liquid distribution trough 8, support frame 10 is used to support Liquid extracting pump 12, is disposed at outside tower body 1 and is easily installed and overhauls.
Embodiment 4:
The separator of hydrocarbon in a kind of separable natural gas as shown in Figure 1:, including tower body 1, packing layer, packing support
Device 3, liquid spraying device and activated carbon treatment device, described filler layer by whole rule filler 4 and dumped packing 5 combination and
At the packing support device 3 is fixed in tower body 1, and described filler layer is deposited on packing support device 3, the liquid spray
The top of packing layer is arranged in shower device, and the activated carbon treatment device is arranged in 1 inner tip of tower body.
The activated carbon treatment device includes: active carbon layer 15, regeneration gas air inlet pipe 14 and regeneration gas escape pipe 19, described
Active carbon layer 15 is fixedly connected on 1 top of tower body, and the regeneration gas air inlet pipe 14 is arranged below active carbon layer 15, the regeneration
Gas escape pipe 19 is arranged above active carbon layer 15, is provided with valve on the regeneration gas air inlet pipe 14 and regeneration gas escape pipe 19
Door 18.By packing layer and with after the liquid reactions in packing layer, major part heavy hydrocarbon therein has been absorbed unstripped gas, but
It is possible or portion of residual heavy hydrocarbon, in order to guarantee de- hydrocarbon rate, active carbon layer 15 is additionally provided with above packing layer, activity
Layer of charcoal 15 is for further absorbing the heavy hydrocarbon in unstripped gas, since the absorption number of active carbon layer 15 is limited, in order to guarantee activity
The absorbability of layer of charcoal 15 is respectively arranged with regeneration gas air inlet pipe 14 and regeneration gas escape pipe in the upper and lower of active carbon layer 15
19, for importing regeneration gas, active carbon layer 15 is regenerated, guarantees the absorbability of active carbon layer 15.
The liquid spraying device includes liquid feed pipe 11, liquid distribution trough 8 and branching block 9, the liquid distribution trough 8
It is fixed in tower body 1, multiple branching blocks 9 is provided on the liquid distribution trough 8, are evenly arranged on the branching block 9 multiple
Aperture, the liquid distribution trough 8 are connected to liquid feed pipe 11.The quality that liquid initial is distributed in packing layer, which not only affects, fills out
The mass-transfer efficiency of material, but also the operating flexibility of filler can be had an impact, therefore in order to reduce by the bad distribution institute of liquid
Caused enlarge-effect gives full play to the efficiency of filler, is provided with liquid distribution trough 8, and liquid distribution trough 8 is mainly uniform by liquid
Ground is sprayed onto packing layer, is connected on liquid distribution trough 8 with liquid feed pipe 11, and liquid feed pipe 11 is for liquid to be imported into
In liquid distribution trough 8, valve 18 is provided on liquid feed pipe 11, for controlling the liquid inlet of liquid feed pipe 11,
In order to further increase the uniformity of liquid sprinkling, it is additionally provided with branching block 9 on liquid distribution trough 8, on the branching block 9
Even to be provided with multiple apertures, liquid is distributed to different zones above packing layer, is uniformly arranged on branching block 9 small by branching block 9
Hole sprays the liquid on packing layer in spraying form, maximumlly to improve the uniformity of liquid sprinkling.
Liquid extracting pump 12,1 outer wall of the tower body setting are provided between the liquid feed pipe 11 and liquid distribution trough 8
There is support frame 10, the Liquid extracting pump 12 is fixed on support frame 10.Liquid extracting pump 12 is for arriving Liquid extracting
In liquid distribution trough 8, support frame 10 is used to support Liquid extracting pump 12, is disposed at outside tower body 1 and is easily installed and overhauls.
Described filler layer is made of the whole rule filler 4 on upper layer and the dumped packing 5 of lower layer, the thickness of the dumped packing 5
It is thicker than the thickness of whole rule filler 4.Filler is one of core component of the present apparatus, is the mass transfer of gas-liquid two-phase contact, and can be made
For heat exchange surface, has and strengthen gas turbulence, reduce the effect of resistance of gas mass transfer, have to the working performance of the present apparatus huge
Influence.Structured packing is by many filler monomer compositions with same geometry, they are loaded in a manner of whole block
In tower, has the advantages that increase gap flow phenomenon rate and effective contact surface area, strengthen empir-ical formulation and the reduction of two-phase
Wall stream and ditch, if using single structured packing, it is not only with high costs, but also limited by flow parameter larger；It is in bulk to fill out
The also known as dumped packings of material 5, have easily fabricated, cheap feature, but only it is single using dumped packing 5 when, liquid
It is unevenly distributed on filling surface, the case where there are wall streams, channel, but also that there are specific surface areas is smaller, voidage is small asks
Topic.The advantages of forming packing layer, can keep two kinds of fillers simultaneously the mode that whole rule filler 4, dumped packing 5 are combined, makes
Disadvantage is complementary, effectively changes the distribution of gas phase and liquid phase, increasing specific surface area and voidage, improves de- hydrocarbon efficiency, and control
Cost.Structured packing has ripple packing, lattices filler and Impulse packing etc., this place uses Corrugated Structured Packings；It is in bulk to fill out
Material 5 has Raschig ring filler, Pall ring filler, saddle class filler, net form filler, cross ring filler etc., this place is filled out using Pall ring
Material.
1 bottom of tower body is provided with air inlet pipe 2, is provided with distribution device in gas-fluid between the air inlet pipe 2 and packing layer
22, liquid re-distributor 7 is provided between described filler layer.After unstripped gas enters tower body 1 out of air inlet pipe 2, it is unevenly distributed,
Contact with packing layer is also insufficient, and in order to improve this status, gas distribution dress is provided between air inlet pipe 2 and packing layer
22 are set, contact uniformity of the unstripped gas with packing layer is improved.And if filler layer depth is blocked up, liquid is easy shape in packing layer
Wall-forming flow phenomenon causes liquid distribution uneven, influences de- hydrocarbon efficiency, in order to avoid this case, two described filler layers it
Between be provided with liquid re-distributor 7, liquid can be equably sprayed onto packing layer by liquid re-distributor 7, improve liquid flow
Distributing homogeneity when to bottom end filler.
Vortex-flow and defrosting device 17 is provided with above the activated carbon treatment device, the vortex-flow and defrosting device 17 is fixedly connected
On 1 inner wall of tower body.Since gas is when tower top leaves packed tower, a large amount of liquid foam and droplet may be had, to recycle this
Partial Liquid Phase is provided with vortex-flow and defrosting device 17 above the activated carbon treatment device, and vortex-flow and defrosting device 17 is by several pieces of fixations
Eddy flow plate composition, when gas passes through, generate rotary motion, cause a centrifugal force field, drop under the action of the centrifugal force, to
Tower wall movement realizes gas-liquid separation.
The bottom of the tower body 1 is provided with liquid reserve tank 23, and the liquid reserve tank 23 is externally connected with acid-proof pump 24.When liquid flows through
Whole packing layers and with after raw material solid/liquid/gas reactions, in liquid contain a large amount of heavy hydrocarbon, need to be collected into this partially liq together simultaneously
It is handled, therefore is fixedly installed liquid reserve tank 23 in the bottom of tower body 1, liquid reserve tank 23 can collect the liquid for flowing to bottom
To together, the liquid with heavy hydrocarbon is discharged in corresponding processing unit by the acid-proof pump 24 being arranged in outside liquid reserve tank 23.
Filler compacting device 6 is provided on the whole rule filler 4 of the top layer of described filler layer.Filler compacting device 6 is installed
It is for keeping packing layer to make for the fixed bed of a height to keep uniform gap structure in packing layer upper end
Operation is normal, stablizes, and prevents when high pressure drop, instantaneous load fluctuation, and packing layer generation loosens or bounce, guarantees this dress
The de- hydrocarbon efficiency set.
It is provided with manhole 21 on the side wall of the tower body 1 and sees inspection window 16.Manhole 21 facilitates maintenance personal to enter in tower body 1
It is overhauled, sees inspection window 16 convenient for the situation in observation tower body 1.
Working principle of the utility model is: raw natural gas enters in tower body 1 from air inlet pipe 2, through distribution device in gas-fluid 22
After distribution, it then is upward through packing layer from the bottom of tower body 1, liquid enters in tower body 1 from liquid feed pipe 11, passes through liquid
Distributor 8 and liquid re-distributor 7 are evenly distributed in packing layer, with upstream raw natural gas in filler surface
Gas-liquid two-phase close contact is reacted, and heavy hydrocarbon therein is absorbed, if the unstripped gas after absorption, which goes back remnants, heavy hydrocarbon, is passed through
Gas tip 13 is directed onto active carbon layer 15 and is absorbed again, may since raw natural gas have passed through a large amount of liquid
With a large amount of liquid foam and droplet, therefore raw natural gas can be such that air-liquid obtains by the vortex-flow and defrosting device 17 at 1 top of tower body
Separation, the gas after separation are entered in lower one for the treatment of process by the escape pipe 20 at 1 top of tower body, and the utility model is mounted on
In skid 25, there is good mobility, the scene that can be thrown at any time after making adequate preparation carries out operation, and above-mentioned liquid uses
Isopentane.
The utility model is not limited to above-mentioned optional embodiment, anyone can obtain under the enlightenment of the utility model
Other various forms of products, however, making any variation in its shape or structure, all the utility model rights that falls into are wanted
The technical solution in confining spectrum is sought, is all fallen within the protection scope of the utility model.
Claims (10)
1. a kind of separator of the hydrocarbon in separable natural gas, it is characterised in that: including tower body (1), packing layer, packing support
Device (3), liquid spraying device and activated carbon treatment device, described filler layer is by whole rule filler (4) and dumped packing (5) group
It closes, the packing support device (3) is fixed in tower body (1), and described filler layer is deposited on packing support device (3),
The top of packing layer is arranged in the liquid spraying device, and the activated carbon treatment device is arranged in tower body (1) inner tip.
2. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: the activity
Charcoal processing unit includes: active carbon layer (15), regeneration gas air inlet pipe (14) and regeneration gas escape pipe (19), the active carbon layer
(15) it is fixedly connected on tower body (1) top, regeneration gas air inlet pipe (14) setting is below active carbon layer (15), the regeneration
Gas escape pipe (19) setting is above active carbon layer (15), on the regeneration gas air inlet pipe (14) and regeneration gas escape pipe (19)
It is provided with valve (18).
3. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: the liquid
Spray equipment includes liquid feed pipe (11), liquid distribution trough (8) and branching block (9), and the liquid distribution trough (8) is fixed on tower
In body (1), it is provided with multiple branching blocks (9), is evenly arranged on the branching block (9) multiple on the liquid distribution trough (8)
Aperture, the liquid distribution trough (8) are connected to liquid feed pipe (11).
4. the separator of the hydrocarbon in a kind of separable natural gas according to claim 3, it is characterised in that: the liquid
Liquid extracting pump (12) is provided between feed pipe (11) and liquid distribution trough (8), tower body (1) outer wall is provided with support frame
(10), the Liquid extracting pump (12) is fixed on support frame (10).
5. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: the tower body
(1) bottom is provided with air inlet pipe (2), is provided with distribution device in gas-fluid (22) between the air inlet pipe (2) and packing layer, described to fill out
Liquid re-distributor (7) are provided between the bed of material.
6. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: the filler
Layer is made of the whole rule filler (4) on upper layer and the dumped packing (5) of lower layer, and the thickness of the dumped packing (5) is thicker than whole rule and fills out
Expect the thickness of (4).
7. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: in the work
Property charcoal processing unit above be provided with vortex-flow and defrosting device (17), the vortex-flow and defrosting device (17) is fixedly connected in tower body (1)
On wall.
8. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: the tower body
(1) bottom is provided with liquid reserve tank (23), and the liquid reserve tank (23) is externally connected with acid-proof pump (24).
9. the separator of the hydrocarbon in a kind of separable natural gas according to claim 5, it is characterised in that: the filler
Filler compacting device (6) are provided on the whole rule filler (4) in upper layer of layer.
10. the separator of the hydrocarbon in a kind of separable natural gas according to claim 1, it is characterised in that: the tower
Manhole (21) He Guanjian window (16) is provided on the side wall of body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822244930.8U CN209307312U (en) | 2018-12-28 | 2018-12-28 | A kind of separator of hydrocarbon in separable natural gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822244930.8U CN209307312U (en) | 2018-12-28 | 2018-12-28 | A kind of separator of hydrocarbon in separable natural gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209307312U true CN209307312U (en) | 2019-08-27 |
Family
ID=67679810
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822244930.8U Expired - Fee Related CN209307312U (en) | 2018-12-28 | 2018-12-28 | A kind of separator of hydrocarbon in separable natural gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209307312U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112300844A (en) * | 2020-11-13 | 2021-02-02 | 大庆市中瑞燃气有限公司 | LNG liquefied heavy hydrocarbon removal method |
-
2018
- 2018-12-28 CN CN201822244930.8U patent/CN209307312U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112300844A (en) * | 2020-11-13 | 2021-02-02 | 大庆市中瑞燃气有限公司 | LNG liquefied heavy hydrocarbon removal method |
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