CN105112114B - One kind set row-tube type gas-liquid separation biogas condenser - Google Patents
One kind set row-tube type gas-liquid separation biogas condenser Download PDFInfo
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- CN105112114B CN105112114B CN201510583628.3A CN201510583628A CN105112114B CN 105112114 B CN105112114 B CN 105112114B CN 201510583628 A CN201510583628 A CN 201510583628A CN 105112114 B CN105112114 B CN 105112114B
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- 239000007788 liquid Substances 0.000 title claims abstract description 60
- 238000000926 separation method Methods 0.000 title claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 46
- 241000521257 Hydrops Species 0.000 claims abstract description 42
- 206010030113 Oedema Diseases 0.000 claims abstract description 42
- 239000012530 fluid Substances 0.000 claims abstract description 34
- 239000003507 refrigerant Substances 0.000 claims abstract description 16
- 230000008676 import Effects 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 238000007689 inspection Methods 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 50
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 210000003128 head Anatomy 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical group C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000005514 two-phase flow Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 210000000795 conjunctiva Anatomy 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000008141 laxative Substances 0.000 description 1
- 230000002475 laxative effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000011176 pooling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
Landscapes
- Separation By Low-Temperature Treatments (AREA)
Abstract
The present invention provides a kind of set row-tube type gas-liquid separation biogas condenser, including the cooling storehouse being detachably connected successively up and down, divide gas storehouse, hydrops storehouse, cooling storehouse sets refrigerant to go out, entrance, several outer tubes are vertically arranged in cooling storehouse, sealed at the top of outer tube, bottom opening passes through the through hole that cooling storehouse bottom is correspondingly arranged and UNICOM of lower floor, divide at the top of gas storehouse and the inner sleeve of socket corresponding with each outer tube is set, the top of inner sleeve open top and the overcoat seal of tube is separately, gas storehouse is divided to include the flow liquid storehouse formed with cooling storehouse bottom interval, and enter gas storehouse positioned at flow liquid storehouse lower floor, inner sleeve bottom opening is through flow liquid storehouse and enters gas storehouse UNICOM；It is hydrops storehouse to enter gas storehouse lower floor；Also include passing vertically through the fluid tube for connecting in flow liquid storehouse with hydrops storehouse into gas storehouse；Condenser structure provided by the invention is simple, compact, and space availability ratio is high, is advantageous to device miniaturization；Each part combines for building block system, is easy to split, and assembles, is advantageous to the maintenance of equipment inspection.
Description
Technical field
It is especially a kind of to cover row-tube type gas-liquid separation biogas condenser the present invention relates to a kind of condenser.
Background technology
At present, biogas condensation liquefaction equipment is general using shell and tube condensing plant conventional now.Traditional tube type cold
Condenser, all it is to condense steam in pipe by refrigerant heat convection outside pipe no matter using the tubulation of which kind of form.Steam is condensing
During, conduct oneself with dignity by the liquid of condensation, vacate position on heat exchange contact surface for steam, reach steam and continue to condense,
So as to realize effect that steam constantly condenses.But in Condensation, as condensate liquid is on the increase, condensate film increases
Thickness, the band that gas-liquid two-phase exchanges mixing can be formed on heat-transfer surface, heat exchange is prevented to a certain extent, under making heat transfer effect drastically
Drop.Then, increasing equipment is usually taken in technique, increases heat exchange area, or takes multistage steam condensation technology, centre is certainly
Take offence liquid isolation technics, concentrate aggregation condensation supercooling technical scheme, eliminate two phase flow.Or exchanged heat using short tube, reduce tube side,
Avoid long tube side from producing condensate liquid conjunctiva, improve heat transfer coefficient, strengthen condensation effect.These schemes be all pack as far as possible it is pure
Steam contacts with heat-transfer surface, eliminates two phase flow and produces.Expected Results is although reached using these schemes, but has also produced and set simultaneously
For the negative effect such as excessive or complicated.
The content of the invention
To solve the above problems, the present invention provides a kind of set row-tube type gas-liquid separation biogas condenser, heat exchange efficiency is high,
Equipment volume is small.
To achieve the above object, the present invention adopts the following technical scheme that：
One kind set row-tube type gas-liquid separation biogas condenser, including be detachably connected successively up and down cooling storehouse 1, divide gas
Storehouse 2, hydrops storehouse 3, the cooling storehouse 1 sets refrigerant entry and exit, several outer tubes 21 is vertically arranged in the cooling storehouse 1, described
The top of outer tube 21 seals, and bottom opening is described to divide gas storehouse 2 by the through hole that the bottom of cooling storehouse 1 is correspondingly arranged and UNICOM of lower floor
Top sets several inner sleeves 22 of socket corresponding with each outer tube 21, and the inner sleeve 22 is sheathed in outer tube 21 and described
The top that the open top of inner sleeve 22 and outer tube 21 seal separately, between the inwall of outer tube 21 and inner sleeve 22 outer wall
Gap is left, described point of gas storehouse 2 includes the interval between the bottom of cooling storehouse 1 and forms flow liquid storehouse 8, and positioned at the lower floor of flow liquid storehouse 8
Enter gas storehouse 9, the bottom opening of inner sleeve 22 through flow liquid storehouse 8 with it is described enter the UNICOM of gas storehouse 9, it is described enter gas storehouse 9 there is air inlet
Mouthful；It is described enter the lower floor of gas storehouse 9 be hydrops storehouse 3；Also include passing vertically through it is described enter gas storehouse 9 flow liquid storehouse 8 is connected with hydrops storehouse 3
Fluid tube 43.
Preferably, the cooling storehouse 1 is cylindrical tank, and the top of cooling storehouse 1 has a hemispherical head 11, described half
The top of dome head 11 is vertically arranged refrigerant exit 14, and the tank base of the cooling storehouse 1 removably connects bottom flange dish
12, the several vertical through holes 13 of the setting of array in the bottom flange dish 12, the corresponding each vertical through hole 13 in the inside of cooling storehouse 1
Position be vertically arranged several outer tubes 21, the top of outer tube 21 seals, lower end outlet welded with bottom flange dish 12 and
Refrigerant import 15 is horizontally disposed with the UNICOM of flow liquid storehouse 8, the bottom sidewall of cooling storehouse 1 by the vertical through hole 13.
Preferably, described point of gas storehouse 2 includes entering gas storehouse 9 by what upper cover plate 41, lower cover 42 and side wall surrounded, it is each it is described in
The bottom opening of sleeve pipe 22 is by the through hole that is correspondingly arranged on the upper cover plate 41 and enters the UNICOM of gas storehouse 9, it is described enter gas storehouse 9 side wall
Set air inlet 5, connected between the upper cover plate 41 and the bottom of cooling storehouse 1 by upper flange plate 44, make the upper cover plate 41 with
Form flow liquid storehouse 8 between the bottom of cooling storehouse 1, the fluid tube 43 is through the upper cover plate 41, lower cover 42 by the flow liquid storehouse 8
With the UNICOM of hydrops storehouse 3.
Preferably, distance is 3-5mm between the outer wall of inner sleeve 22 and outer tube 21 inwall.
Preferably, it is described enter gas storehouse 9 sidewall symmetry set at least two horizontal directions air inlet 5.
Preferably, more of the setting of the array of fluid tube 43.
Preferably, by being fixed on the laxative remedy into the bottom of lower cover 42 of gas storehouse 9 between described point of gas storehouse 2 and hydrops storehouse 3
Blue disk 45 is detachably connected.
Preferably, the hydrops storehouse 3 is hemispherical tank body, and the hydrops storehouse 3 is provided with gas returning port 31, the gas returning port 31
The horizontally disposed upper side of hydrops storehouse 3, the gas returning port 31 are connected by pipeline with the air inlet 5 of point gas storehouse 2, the hydrops
The bottom of storehouse 3 is additionally provided with fluid port 32.
Preferably, fluid reservoir 10 is also included, the fluid reservoir 10 includes tank body, and both sides set first at the top of the tank body
Inlet 101, the second inlet 102, the tank base set leakage fluid dram 103, and second inlet 102 connects a leakage
Choke tube 104, the leakage choke tube 104 are made up of threeway 105, bend pipe 106 and ring flange 107, the upper port of threeway 105
It is connected with the bottom fluid port 32 of hydrops storehouse 3, is connected between the lower port of threeway 105 and first inlet 101 by ball valve
Connect, the middle port of threeway 105 is connected with the bend pipe 106；The outlet of bend pipe 106 sets ring flange 107.
The beneficial effects of the present invention are：It is provided by the invention set row-tube type gas-liquid separation biogas condenser with it is normal now
See that traditional shell and tube gas-liquid separation condenser is compared, not only make use of the principle of liquid deadweight sinking after liquefaction, also use interior
The progradation of flowing gas in gap between outer tube, the gas-liquid mixed layer in liquefaction face is removed in time, tubulation is improved and changes
The thermal efficiency；The inner sleeve of the condenser of the present invention, set outer tube intercommunication, simple in construction, compact, space availability ratio is higher, is advantageous to
The miniaturization of refrigeration plant；Each part combines for building block system, can split whenever and wherever possible, assembles, and is advantageous to equipment inspection
Look into and repair.
Brief description of the drawings
Fig. 1 is specific embodiment of the invention part-structure schematic diagram；
Fig. 2 is Section A-A schematic diagram in Fig. 1；
Fig. 3 is that the embodiment of the present invention enters the structural representation of gas storehouse upper cover plate 41；
Fig. 4 is that the embodiment of the present invention enters the structural representation of gas storehouse lower cover 42；
Fig. 5 is specific embodiment of the invention overall structure diagram.
Label in figure：1- cooling storehouses, 2- points of gas storehouse, 3- hydrops storehouse, 21- outer tubes, 22- inner sleeves, 8- flow liquids storehouse, 9- enter
Gas storehouse, 43- fluid tubes, 11- hemispherical heads, 14- refrigerant exits, 12- bottom flange dish, the vertical through holes of 13-, 15- refrigerants enter
Mouth, 41- upper cover plates, 42- lower covers, 5- air inlets, 44- upper flange plates, 45- lower flanges, 31- gas returning ports, 32- fluid ports,
10- fluid reservoirs, the inlets of 101- first, the inlets of 102- second, 103- leakage fluid drams, 104- leakages choke tube, 105- threeways,
106- bend pipes, 107- ring flanges.
Embodiment
In order to facilitate the understanding of the purposes, features and advantages of the present invention, below in conjunction with the accompanying drawings to the present invention
Embodiment be described in detail.
Many details are elaborated in the following description to facilitate a thorough understanding of the present invention, still the present invention can be with
It is different from other manner described here using other to implement, those skilled in the art can be without prejudice to intension of the present invention
In the case of do similar popularization, therefore the present invention is not limited by following public specific embodiment.
Secondly, combination schematic diagram of the present invention is described in detail, when the embodiment of the present invention is described in detail, for purposes of illustration only, table
The profile of showing device structure can disobey general proportion and make partial enlargement, and the schematic diagram is example, and it should not herein
Limit the scope of protection of the invention.In addition, the three-dimensional space of length, width and depth should be included in actual fabrication.
As shown in figure 1, the present embodiment provides a kind of set row-tube type gas-liquid separation biogas condenser, including successively may be used up and down
The cooling storehouse 1 of dismantling connection, divide gas storehouse 2, hydrops storehouse 3, the cooling storehouse 1 sets refrigerant entry and exit, erected in the cooling storehouse 1
Several outer tubes 21 are directly set, and the top of outer tube 21 seals, the through hole that bottom opening is correspondingly arranged by the bottom of cooling storehouse 1
With UNICOM of lower floor, the several inner sleeves 22 for dividing the top of gas storehouse 2 to set socket corresponding with each outer tube 21, the inner sleeve 22
It is sheathed on top that in outer tube 21 and the open top of inner sleeve 22 seals with outer tube 21 separately, the outer tube 21
Gap is left between inwall and the outer wall of inner sleeve 22, distance is 3-5mm between the outer wall of inner sleeve 22 and outer tube 21 inwall.
Specifically, as shown in figure 1, the cooling storehouse 1 is cylindrical tank, the top of cooling storehouse 1 has hemispherical head 11, described
The top of hemispherical head 11 is vertically arranged refrigerant exit 14, as shown in Fig. 2 the tank base of the cooling storehouse 1 removably connects
Connect bottom flange dish 12, the several vertical through holes 13 of the setting of array in the bottom flange dish 12, the inside of cooling storehouse 1 is corresponding
The position of each vertical through hole 13 is vertically arranged several outer tubes 21, and the top of outer tube 21 seals, lower end outlet and bottom method
Blue disk 12 welds and by the vertical through hole 13 and the UNICOM of flow liquid storehouse 8, the bottom sidewall of cooling storehouse 1 is horizontally disposed with cold
Matchmaker's import 15.Described point of gas storehouse 2 includes the flow liquid storehouse 8 formed with the bottom interval of cooling storehouse 1, and entering positioned at the lower floor of flow liquid storehouse 8
Gas storehouse 9, the bottom opening of inner sleeve 22 through flow liquid storehouse 8 with it is described enter the UNICOM of gas storehouse 9, it is described enter gas storehouse 9 there is air inlet；
It is described enter the lower floor of gas storehouse 9 be hydrops storehouse 3；Also include passing vertically through it is described enter the stream that connects in flow liquid storehouse 8 with hydrops storehouse 3 of gas storehouse 9
Liquid pipe 43, specifically, by being fixed on the lower flange into the bottom of lower cover 42 of gas storehouse 9 between described point of gas storehouse 2 and hydrops storehouse 3
Disk 45 is detachably connected, and in the present embodiment, is detachably connected by ring flange between the cooling storehouse 1, point gas storehouse 2, hydrops storehouse 3
Connect, be easy to the maintenance and replacing of equipment room.
Specifically, as shown in Fig. 1, Fig. 3-Fig. 4, described point of gas storehouse 2 includes being surrounded by upper cover plate 41, lower cover 42 and side wall
Enter gas storehouse 9, each bottom opening of inner sleeve 22 is by the through hole that is correspondingly arranged on the upper cover plate 41 and enters gas storehouse 9
It is logical, it is described enter gas storehouse 9 side wall air inlet 5 is set, further, it is described enter gas storehouse 9 sidewall symmetry at least two water are set
Square to air inlet 5, connected between the upper cover plate 41 and the bottom of cooling storehouse 1 by upper flange plate 44, make the upper cover plate
Form flow liquid storehouse 8 between 41 and the bottom of cooling storehouse 1, the fluid tube 43 is through the upper cover plate 41, lower cover 42 by the stream
Liquid storehouse 8 and the UNICOM of hydrops storehouse 3, the fluid tube 43 can array more of setting, passed through for inner sleeve 22 on the upper cover plate 41
Through hole and fluid tube 43 export spaced array and set, in the present embodiment, by mutually being covered between outer tube 21 and inner sleeve 22
Connect, reduce the volume of whole equipment, but the heat exchange area of biogas is relatively large, and coolant can utilize self gravitation downward
Lamination liquid storehouse 3 deposits, and heat exchange efficiency is higher.
Specifically, the hydrops storehouse 3 is hemispherical tank body, the hydrops storehouse 3 is provided with gas returning port 31, the gas returning port 31
The horizontally disposed upper side of hydrops storehouse 3, the gas returning port 31 are connected by pipeline with the air inlet 5 of point gas storehouse 2, the hydrops
The bottom of storehouse 3 is additionally provided with fluid port 32.
Further, as shown in figure 5, also including fluid reservoir 10, the fluid reservoir 10 includes tank body, the tank body top
Both sides set the first inlet 101, the second inlet 102, and the tank base sets leakage fluid dram 103, second inlet
102 one leakage choke tubes 104 of connection, the leakage choke tube 104 is made up of threeway 105, bend pipe 106 and ring flange 107, described
The upper port of threeway 105 is connected with the bottom fluid port 32 of hydrops storehouse 3, the lower port of threeway 105 and first inlet 101 it
Between connected by ball valve, the middle port of threeway 105 is connected with the bend pipe 106；The outlet of bend pipe 106 sets ring flange
107, the threeway 105 of leakage choke tube 104 is suitable for reading to be connected with hydrops orlop portion fluid port 32, and lower mouth is connected with ball valve, and is connected
First inlet 101 of fluid reservoir 10, another mouth are connected with bend pipe 106, and the bend pipe makes choke tube highly carry by 90 degree of elbows
The upper limit liquid level of hydrops storehouse 3 is risen to, and 90 degree of elbows are being used near upper limit liquid level, bend pipe is bent in the horizontal direction, and
Exit mounting flange 107, to be connected with other pipelines, the second inlet 102 of fluid reservoir 10 is connected in the present embodiment.
Specifically, because biogas main component is methane, its normal pressure condensing temperature is -162 DEG C.It is biogas liquefied in order to realize
And pooling function, all devices of the present invention are adiabatic using insulating.
The operation principle and workflow for the set row-tube type gas-liquid separation condenser that the present embodiment provides are as follows：
Purifying marsh gas to be liquefied enters from the air inlet of gas storehouse 9 that enters of point gas storehouse 2, and in air inlet under the driving of itself air pressure
By upper cover plate 41 and the circular hole of inner sleeve 22 in storehouse 9, enter in each inner sleeve 22；What the biogas of inner sleeve 22 was delivered up
Cooled down simultaneously, then by the top down of the outer tube 21 backflow further cooling of top seal, liquefaction；Simultaneously refrigerant from
The refrigerant import 15 of cooling storehouse 1 inputs, and is exported from refrigerant exit 14, so as to which the heat in cooling storehouse 1 be taken away, realizes outer tube
22nd, gas liquefaction in inner sleeve 21；Specifically, the refrigerant also compressed nitrogen, the biogas after liquefaction, in the top source of outer tube 21
In the presence of the promotion and deadweight of the biogas that source continually enters, flow downward, be cooled to -130 DEG C, and during flowing downward
Continue to liquefy, liquefied biogas and not liquefied cooling biogas, enter flow liquid storehouse 8 from the lower outlet of outer tube 21, then pass through
Fluid tube 43 enters in hydrops storehouse 3；In hydrops storehouse 3, liquefied biogas is gathered in the bottom of hydrops storehouse 3 under Gravitative Loads, and
Progressively flow to leakage choke tube 104 and fluid reservoir 10, and not liquefied cooling gas, pass through what the top sidewall of hydrops storehouse 3 was set
Gas returning port 31, the air inlet 5 into gas storehouse 9 is back to, goes successively to cooling liquid flow.The effect of leakage choke tube 104 is,
When liquid level rises to 3 upper limit liquid level of hydrops storehouse, liquid flows out from the ring flange 107 of the curved 104 pipe upper end of choke, enters by second
Liquid mouth 102 enters fluid reservoir 10.
Although the present invention is disclosed as above with preferred embodiment, but is not limited to the present invention.It is any to be familiar with ability
The technical staff in domain, without departing from the scope of the technical proposal of the invention, all using in the methods and techniques of the disclosure above
Appearance makes many possible changes and modifications to technical solution of the present invention, or is revised as the equivalent embodiment of equivalent variations.Therefore,
Every content without departing from technical solution of the present invention, the technical spirit according to the present invention is to made for any of the above embodiments any simple
Modification, equivalent variations and modification, in the range of still falling within technical solution of the present invention protection.
Claims (8)
1. one kind set row-tube type gas-liquid separation biogas condenser, it is characterised in that cold including what is be detachably connected successively up and down
But storehouse (1), divide gas storehouse (2), hydrops storehouse (3), the cooling storehouse (1) sets refrigerant entry and exit, vertical in the cooling storehouse (1)
Several outer tubes (21) are set, sealed at the top of the outer tube (21), bottom opening is correspondingly arranged by cooling storehouse (1) bottom
Through hole and UNICOM of lower floor, it is described to divide at the top of gas storehouse (2) several inner sleeves (22) that socket corresponding with each outer tube (21) is set, institute
State inner sleeve (22) and be sheathed on the top that in outer tube (21) and inner sleeve (22) open top seals with outer tube (21)
Separately, gap is left between outer tube (21) inwall and inner sleeve (22) outer wall；Described point of gas storehouse (2) includes and cooling
The flow liquid storehouse (8) formed between storehouse (1) bottom, and enter gas storehouse (9), inner sleeve (22) bottom positioned at flow liquid storehouse (8) lower floor
Portion's opening through flow liquid storehouse (8) with it is described enter gas storehouse (9) UNICOM, it is described enter gas storehouse (9) there is air inlet；It is described enter gas storehouse (9)
Lower floor is hydrops storehouse (3)；Also include passing vertically through it is described enter gas storehouse (9) fluid tube that connects flow liquid storehouse (8) with hydrops storehouse (3)
(43)；The hydrops storehouse (3) is hemispherical tank body, and the hydrops storehouse (3) is provided with gas returning port (31), gas returning port (31) water
Flat to set hydrops storehouse (3) upper side, the gas returning port (31) is connected by pipeline with the air inlet (5) of a point gas storehouse (2), institute
State hydrops storehouse (3) bottom and be additionally provided with fluid port (32).
A kind of 2. set row-tube type gas-liquid separation biogas condenser as claimed in claim 1, it is characterised in that the cooling storehouse
(1) it is cylindrical tank, cooling storehouse (1) top has hemispherical head (11), and hemispherical head (11) top is erected
It is straight that refrigerant exit (14), the detachably connected bottom flange dish of tank base (12) of the cooling storehouse (1), the bottom are set
Several vertical through holes (13) are set in array on ring flange (12), each vertical through hole (13) is corresponded to inside the cooling storehouse (1)
Position is vertically arranged several outer tubes (21), is sealed at the top of the outer tube (21), and lower end outlet is welded with bottom flange dish (12)
Connect and refrigerant is horizontally disposed with flow liquid storehouse (8) UNICOM, cooling storehouse (1) bottom sidewall by the vertical through hole (13)
Import (15).
3. a kind of set row-tube type gas-liquid separation biogas condenser as claimed in claim 1, it is characterised in that described to divide gas storehouse
(2) include entering gas storehouse (9), each inner sleeve (22) bottom opening by what upper cover plate (41), lower cover (42) and side wall surrounded
By the through hole that is correspondingly arranged on the upper cover plate (41) and enter gas storehouse (9) UNICOM, it is described enter gas storehouse (9) side wall air inlet is set
Mouth (5), is connected by upper flange plate (44) between the upper cover plate (41) and cooling storehouse (1) bottom, makes the upper cover plate (41)
Flow liquid storehouse (8) are formed between cooling storehouse (1) bottom, the fluid tube (43) passes through the upper cover plate (41), lower cover (42)
By the flow liquid storehouse (8) and hydrops storehouse (3) UNICOM.
As claimed in claim 3 a kind of 4. set row-tube type gas-liquid separation biogas condenser, it is characterised in that it is described enter gas storehouse
(9) sidewall symmetry sets the air inlet (5) of at least two horizontal directions.
A kind of 5. set row-tube type gas-liquid separation biogas condenser as claimed in claim 3, it is characterised in that the fluid tube
(43) more of the setting of array.
6. a kind of set row-tube type gas-liquid separation biogas condenser as claimed in claim 3, it is characterised in that described to divide gas storehouse
(2) detachably connected by the lower flange (45) being fixed on into lower cover (42) bottom of gas storehouse (9) between hydrops storehouse (3)
Connect.
A kind of 7. set row-tube type gas-liquid separation biogas condenser as claimed in claim 1, it is characterised in that the inner sleeve
(22) distance is 3-5mm between outer wall and outer tube (21) inwall.
8. a kind of set row-tube type gas-liquid separation biogas condenser as claimed in claim 1, it is characterised in that also include storage
Flow container (10), the fluid reservoir (10) include tank body, and both sides set the first inlet (101), the second feed liquor at the top of the tank body
Mouth (102), the tank base set leakage fluid dram (103), and second inlet (102) connects a leakage choke tube (104),
The leakage choke tube (104) is made up of threeway (105), bend pipe (106) and ring flange (107), threeway (105) upper port
It is connected with hydrops storehouse (3) bottom fluid port (32), leads between threeway (105) lower port and first inlet (101)
Ball valve connection is crossed, threeway (105) middle port is connected with the bend pipe (106)；Bend pipe (106) outlet sets ring flange
(107)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510583628.3A CN105112114B (en) | 2015-09-15 | 2015-09-15 | One kind set row-tube type gas-liquid separation biogas condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510583628.3A CN105112114B (en) | 2015-09-15 | 2015-09-15 | One kind set row-tube type gas-liquid separation biogas condenser |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105112114A CN105112114A (en) | 2015-12-02 |
| CN105112114B true CN105112114B (en) | 2017-11-14 |
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ID=54660236
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|---|---|---|---|
| CN201510583628.3A Active CN105112114B (en) | 2015-09-15 | 2015-09-15 | One kind set row-tube type gas-liquid separation biogas condenser |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108467825B (en) * | 2018-06-29 | 2023-06-30 | 青岛涌略环境科学研究院有限公司 | Rapid dry anaerobic reaction device for household garbage |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB273298A (en) * | 1926-06-25 | 1927-11-03 | Einar Morterud | Improvements relating to liquid heaters and evaporators |
| SE366388B (en) * | 1972-05-05 | 1974-04-22 | Svenska Maskinverken Ab | |
| FI76699C (en) * | 1986-06-25 | 1988-12-12 | Ahlstroem Oy | INDUNSTARE AV ROERTYP. |
| CA2036494C (en) * | 1990-05-11 | 1995-06-27 | Tai W. Kwok | Heat exchanger in an hf alkylation process |
| CN205062015U (en) * | 2015-09-15 | 2016-03-02 | 海南北鸥生物能源开发有限公司 | Sleeve pipe shell and tube gas -liquid separation marsh gas condenser |
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2015
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| CN105112114A (en) | 2015-12-02 |
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