CN107308676A - Vertical condensation device - Google Patents
Vertical condensation device Download PDFInfo
- Publication number
- CN107308676A CN107308676A CN201710607915.2A CN201710607915A CN107308676A CN 107308676 A CN107308676 A CN 107308676A CN 201710607915 A CN201710607915 A CN 201710607915A CN 107308676 A CN107308676 A CN 107308676A
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- Prior art keywords
- cylinder
- vertical condensation
- outlet
- chamber
- air inlet
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
- B01D5/0012—Vertical tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0036—Multiple-effect condensation; Fractional condensation
Abstract
The present invention relates to condensation process technical field, a kind of vertical condensation device is disclosed.Vertical condensation device includes the drain pan for being formed with liquid storage cylinder；Air inlet vertical condensation cylinder and outlet vertical condensation cylinder are vertically arranged on the upper shell wall of drain pan respectively, air inlet vertical condensation cylinder includes the inlet chamber with air inlet and the cooling chamber with inlet and liquid outlet, outlet vertical condensation cylinder includes the outlet chamber with gas outlet and the cooling chamber with inlet and liquid outlet, it is respectively separated in the cooling chamber of air inlet vertical condensation cylinder and outlet vertical condensation cylinder and is vertically arranged with many tracheaes, the upper end of many tracheaes in air inlet vertical condensation cylinder is connected with inlet chamber and lower end is connected with liquid storage cylinder, the upper end of many tracheaes in outlet vertical condensation cylinder is connected with outlet chamber and lower end is connected with liquid storage cylinder.The vertical condensation device of the present invention is while realizing that gas-liquid mixture is efficiently separated, and floor space is smaller, and can as needed ask and be easy to be moved to required occasion.
Description
Technical field
The present invention relates to condensation process technical field, in particular it relates to which a kind of vertical condensation device, divides for gas-liquid
From.
Background technology
For example in petroleum industry, greasy dirt discarded object produced when oilfield exploitation, oil plant production, oil can be produced
Store high pollution discarded object that the tank bottom greasy dirt discarded object produced and petroleum and petrochemical sector, steel mill are produced etc..These are discarded
Thing discharge can serious pollution is caused to surrounding environment, from and dangerous waste species have been included in by country.To prevent Polluted Soil
Earth, water body and air etc., it is necessary to handle these discarded objects in time.In addition, these discarded object amounts are big, wherein can profit containing certain
With the petroleum resources and other energy (for example, heat energy) of value.Respond the strategy of sustainable development, recycling of recyclable waste with goods and materials not
The disconnected Economic Development Mode recycled is global trend, it is therefore desirable to the regenerative resource in recycling the waste.In a word, for
Above-mentioned discarded object, should realize environmental protection, and the purpose of resource recycling is reached again.
Developed the processing methods of a variety of greasy dirt discarded objects at present, for example, concentration desiccation method, flotation go oil process,
Viscosity reduction filter press technique, extraction separation method, microbial degradation method, centrifugal separation, direct landfill method, helical feed continuous treatment process
Deng.These methods can all use all condensing units substantially, to realize the separation of gas-liquid.
At present, existing condensing unit is all horizontal condenser, and this horizontal condenser floor space is larger, and due to
Chassis is larger and can not easily be moved according to the demand of actual use occasion.
The content of the invention
It is an object of the invention to provide a kind of vertical condensation device, the vertical condensation installation area is smaller, and energy
Enough ask as needed is easy to be moved to required occasion.
In order to achieve the above object, the present invention provides a kind of vertical condensation device, including：Formed in drain pan, the drain pan
There is liquid storage cylinder；Air inlet vertical condensation cylinder and outlet vertical condensation cylinder, the air inlet vertical condensation cylinder and the outlet vertical condensation
Cylinder is vertically arranged on the upper shell wall of the drain pan respectively, air inlet vertical condensation cylinder include inlet chamber with air inlet and
Cooling chamber with inlet and liquid outlet, the outlet vertical condensation cylinder includes the outlet chamber with gas outlet and with feed liquor
The cooling chamber of mouth and liquid outlet, wherein, difference in the cooling chamber of the air inlet vertical condensation cylinder and outlet vertical condensation cylinder
Be spaced and be vertically arranged with many tracheaes, wherein, the upper end of many tracheaes in air inlet vertical condensation cylinder with it is described
Inlet chamber is connected and lower end connect with the liquid storage cylinder, the upper end of many tracheaes in the outlet vertical condensation tin and
The outlet chamber is connected and lower end is connected with the liquid storage cylinder.
By the technical scheme, due to storage cooling water using the condensation tube that is cooled down to endotracheal gas-liquid mixture as
It is vertical and arranged along short transverse, so, relative to prior art it is horizontal for, this vertical condensation cylinder can be effectively
The space above drain pan is utilized, it is to avoid take more horizontal area, simultaneously as many tracheaes in air inlet vertical condensation cylinder
Upper end connected with inlet chamber and lower end is connected with liquid storage cylinder, meanwhile, the upper end of many tracheaes in outlet vertical condensation cylinder
Connected with outlet chamber and lower end is connected with liquid storage cylinder, the gas mixture entered by air inlet in inlet chamber will be by entering
Many tracheaes in gas vertical condensation cylinder flow downward, while under the cooling of cooling water, will condense to form profit in tracheal strips
Mixture is simultaneously dropped onto in liquid storage cylinder along tracheae, then, and many gas in outlet vertical condensation cylinder are flowed into by liquid storage cylinder
Manage and the water cooling formation oil water mixture that is cooled, and be flowed into along tracheae in liquid storage cylinder, subsequent gas is flowed into outlet chamber
It is interior and from gas outlet outflow, so, vertical condensation device of the invention while realizing that gas-liquid mixture is efficiently separated, take up an area
Area is smaller, and can as needed ask and be easy to be moved to required occasion.
Further, at least one described tracheal strips is provided with the spiral guide sheet along the axial direction extension of pipe, with institute
State the passage that tracheal strips formation is extended spirally.
Further, the thickness of the spiral guide sheet is 1mm-3mm.
In addition, being provided with dividing plate in the drain pan, the liquid storage cylinder is divided into upper chambers and lower chamber by the dividing plate, its
In, the lower end of many tracheaes in the air inlet vertical condensation cylinder is connected with the upper chambers, the outlet vertical condensation
The lower end of many tracheaes in cylinder is connected with the upper chambers, and is provided between the upper chambers and the lower chamber
Switch valve.
Further, the dividing plate is in tilted layout towards the switch valve.
In addition, the top of the lower chamber is provided with air bleeding valve, and the bottommost of the lower chamber is provided with control valve.
In addition, in the liquid storage cylinder, being provided with the upper shell wall of the liquid storage cylinder positioned at air inlet vertical condensation cylinder
Flow-stopping plate between the outlet vertical condensation cylinder, wherein, under many tracheaes in the air inlet vertical condensation cylinder
The chamber connected between end and the lower end of many tracheaes in outlet vertical condensation cylinder is following with the flow-stopping plate
Air guide interval is formed between edge.
Further, the flow-stopping plate is multiple, and along gas flow direction, the height of the flow-stopping plate of upstream is more than
The height of the flow-stopping plate in downstream.
In addition, the air inlet vertical condensation cylinder and the respective inlet of outlet vertical condensation cylinder are located at cylinder bottom simultaneously
It is connected with total feed tube；The air inlet vertical condensation cylinder and the respective liquid outlet of outlet vertical condensation cylinder are located at cylinder top
And it is connected with main drain pipe.
In addition, being respectively arranged with folding in the air inlet vertical condensation cylinder and the respective cooling chamber of outlet vertical condensation cylinder
Flow plate.
Brief description of the drawings
Accompanying drawing is, for providing a further understanding of the present invention, and to constitute a part for specification, with following tool
Body embodiment is used to explain the present invention together, but is not construed as limiting the invention.In the accompanying drawings：
Fig. 1 is the structural representation of the side for the vertical condensation device that the specific embodiment of the invention is provided；
Fig. 2 be Fig. 1 vertical condensation device in tracheae broken section structural representation；
Fig. 3 is the schematic diagram of spiral guide sheet in Fig. 2.
Description of reference numerals
27- drain pans, 28- liquid storage cylinders, 29- air inlets vertical condensation cylinder, 30- inlets, 31- liquid outlets, 32- cooling chambers, 33-
Tracheae, 34- outlets vertical condensation cylinder, 35- spiral guide sheets, 36- dividing plates, 37- upper chambers, 38- lower chambers, 39- switch valves, 40-
Total feed tube, 41- main drain pipes, 42- inlet chambers, 43- outlet chambers, 44- flow-stopping plates, 45- deflection plates, 46- control valves.
Embodiment
The embodiment of the present invention is described in detail below in conjunction with accompanying drawing.It should be appreciated that this place is retouched
The embodiment stated is merely to illustrate and explain the present invention, and is not intended to limit the invention.
Reference picture 1, it is vertical that the vertical cooling device that the present invention is provided includes drain pan 27, air inlet vertical condensation cylinder 29, outlet
Condensation tube 34 and Duo Gen tracheaes 33, wherein, liquid storage cylinder 28 is formed with drain pan 27, is mixed with storing the profit after such as Oil-gas Separation
Compound；Air inlet vertical condensation cylinder 29 and outlet vertical condensation cylinder 34 are vertically arranged on the upper shell wall of drain pan 27 respectively, and air inlet is stood
Formula condensation tube 29 includes the inlet chamber 42 with air inlet and the cooling chamber 32 with inlet 30 Yu liquid outlet 31, and outlet is vertical
Condensation tube includes the outlet chamber 43 with gas outlet and the cooling chamber 32 with inlet 30 Yu liquid outlet 31, such as, outside
Chilled water unit provides cooling water by inlet 30 into cooling chamber 32；Air inlet vertical condensation cylinder 29 and outlet vertical condensation cylinder
It is respectively separated in 34 cooling chamber 32 and is vertically arranged with many tracheaes 33 (being condenser pipe), wherein, air inlet vertical condensation cylinder
The upper end of many tracheaes 33 in 29 is connected with inlet chamber 42 and lower end is connected with liquid storage cylinder 28, in outlet vertical condensation cylinder 34
The upper ends of many tracheaes 33 connected with outlet chamber 43 and lower end is connected with liquid storage cylinder 28.
In the technical scheme, due to storage cooling water using the condensation tube that is cooled down to endotracheal gas-liquid mixture as
It is vertical and arranged along short transverse, so, relative to prior art it is horizontal for, this vertical condensation cylinder can be effectively
The space above drain pan is utilized, it is to avoid take more horizontal area, simultaneously as many tracheaes in air inlet vertical condensation cylinder
Upper end connected with inlet chamber and lower end is connected with liquid storage cylinder, meanwhile, the upper end of many tracheaes in outlet vertical condensation cylinder
Connected with outlet chamber and lower end is connected with liquid storage cylinder, the gas mixture entered by air inlet in inlet chamber will be by entering
Many tracheaes in gas vertical condensation cylinder flow downward, while under the cooling of cooling water, will condense to form profit in tracheal strips
Mixture is simultaneously dropped onto in liquid storage cylinder along tracheae, then, and many gas in outlet vertical condensation cylinder are flowed into by liquid storage cylinder
Manage and the water cooling formation oil water mixture that is cooled, and be flowed into along tracheae in liquid storage cylinder, subsequent gas is flowed into outlet chamber
It is interior and from gas outlet outflow, so, vertical condensation device of the invention while realizing that gas-liquid mixture is efficiently separated, take up an area
Area is small, and condensation effect is very good, and condensation efficiency is high, convenient disassembly, is easy to safeguard, is particularly suitable for skid movement and uses.
In addition, the oil gas separation in order to lift gas mixture, it is preferable that as illustrated in fig. 1 and 2, at least one
The spiral guide sheet 35 along the axial direction extension of pipe is provided with tracheae 33, to form the passage extended spirally in tracheae 33,
So, oil-gas mixer flows the passage extended spirally formed along spiral guide sheet 35, and this can significantly lift oil gas
The stroke that mixture is advanced, more to be exchanged heat with cooling water, meanwhile, this will also be significantly reduced air inlet vertical condensation 29 Hes of cylinder
The length of outlet vertical condensation cylinder 34, further, since the passage extended spirally, can cause gas mixture to form a kind of eddy flow
And stir, it is easier to the gas mixture at the middle part of tracheae 33 carries out heat exchange.
Certainly, the width of spiral guide sheet 35 can be equal to the diameter of tracheae, might be less that the direct of tracheae, such as be equal to
The radius of tracheae.
In addition, for the ease of the dismounting of spiral guide sheet 35, it is preferable that spiral guide sheet 35 is provided at both ends with branch pipe.So,
It can realize that spiral guide sheet 35 is easily assembled to tracheal strips, or take out from tracheal strips by acting on branch pipe.
Certainly, the thickness of spiral guide sheet 35 can be selected according to demand, such as, can be 1-3mm, or, more preferably
Ground, is 2mm.
In addition, as shown in Figure 1, dividing plate 36 is provided with drain pan 27, liquid storage cylinder 28 is divided into upper chambers 37 by dividing plate 36
With lower chamber 38, wherein, the lower end of many tracheaes 33 in air inlet vertical condensation cylinder 29 is connected with upper chambers 37, and outlet is vertical cold
The lower end of many tracheaes 33 in solidifying cylinder 34 is connected with upper chambers 37 so that upper chambers 37 be used for temporary transient oil in reserve liquid mixture with
It is easy to gas to circulate, and switch valve 39 is provided between upper chambers 37 and lower chamber 38.So, the oil that each tracheal strips condenses
Aqueous mixtures will be dripped and had previously been stored in upper chambers 37, due to the different densities of profit, and oil will be swum on the water surface with reality
Existing pre-separation, gather it is a certain amount of after, open switch valve 39, the water section of bottom can be put into lower chamber 38 to store up
Deposit, and the liquid level in lower chamber 38 is when reaching predetermined value, can empty the gas port in lower chamber 38 with closing switch valve 39,
Oil water mixture is transported in oil-water separation system 2 and carries out thoroughly water-oil separating, and the fluid floated in upper chambers 37 is then
Can extract, or, upper chambers 37 be stored into it is a certain amount of after, open switch valve 39, oil water mixture is put into bottom
With standing in chamber 38 so that fluid is floated on the water surface.The unlatching of switch valve 39 can also be remained, makes oil mixing with water logistics
Move in lower chamber 38, with static separation oil and water.
In addition, for the ease of the water of the inner bottom part of upper chambers 37 is put into lower chamber 38, it is preferable that dividing plate 36 is towards opening
Close valve 39 to be in tilted layout, so, open after switch valve 39, the water of bottom just more likely can be flowed into lower chamber 38 more,
And the oil floated can then stay in upper chambers 37 to carry out subsequent treatment.
Further, the top of lower chamber 38 is provided with air bleeding valve, to discharge the gas leaked into lower chamber 38, bottom
The bottommost of chamber 38 is provided with control valve 46, so, and liquid is stored in lower chamber 38 to be discharged by control valve 46, so as to
In follow-up purified treatment, and the fluid floated then can be by collecting after being flowed out after water is discharged by control valve 46.
In addition, as shown in Figure 1, in order to further lift oil gas separation, it is preferable that in liquid storage cylinder 28, liquid storage
The flow-stopping plate 44 between air inlet vertical condensation cylinder 29 and outlet vertical condensation cylinder 34 is provided with the upper shell wall of chamber 28, its
In, the lower end and the lower end of many tracheaes 33 in outlet vertical condensation cylinder 34 of many tracheaes 33 in air inlet vertical condensation cylinder 29
Between the chamber (inner surface of the lower shell wall of such as liquid storage cylinder 28 or the upper surface towards upper chambers 37 of dividing plate 36) that connects
Air guide interval is formed between the lower edge of flow-stopping plate 44.So, the lower end of many tracheaes 33 in air inlet vertical condensation cylinder 29
The air impingement of discharge is on flow-stopping plate 44 so that the part oil in gas is sticked on the side of flow-stopping plate 44, then from leading
The many tracheal strips that gas interval is flowed through and is flowed into outlet vertical condensation cylinder 34.
Further, as shown in Figure 1, flow-stopping plate 44 is multiple, and along gas flow direction, the flow-stopping plate of upstream
44 height is more than the height of the flow-stopping plate 44 in downstream.So, the flow-stopping plate 44 of upstream stops gas, adhesion part oil first
Gas, the flow-stopping plate 44 will be bypassed by subsequently passing through the gas at the air guide interval of the lower section of the flow-stopping plate 44 of upstream, and strike downstream
On shorter flow-stopping plate 44, and adhere to a part of oil gas.
In addition, for further improving heat exchanging efficiency, it is ensured that enter air inlet vertical condensation cylinder 29 and outlet is vertical cold
The initial temperature of cooling water in solidifying cylinder 34 is relatively low, lifts condensation effect, air inlet vertical condensation cylinder 29 and outlet vertical condensation cylinder
34 respective inlets 30 are located at cylinder bottom and are connected with total feed tube 40；Air inlet vertical condensation cylinder 29 and outlet vertical condensation
34 respective liquid outlets 31 of cylinder are located at cylinder top and are connected with main drain pipe 41.So, the cooling water that total feed tube 40 is provided
It will be split and enter in air inlet vertical condensation cylinder 29 and outlet vertical condensation cylinder 34, and from the row of main drain pipe 41 after heat exchange
Go out.
In addition, the heat transfer effect in order to lift the condensed water in air inlet vertical condensation cylinder 29 and outlet vertical condensation cylinder 34,
Avoid occurring heat exchanging corner between condensed water and tracheae, it is preferable that as shown in Figure 1, air inlet vertical condensation cylinder 29 and outlet are vertical
Deflection plate 45 is respectively arranged with the respective cooling chamber 32 of formula condensation tube 34.So, by deflection plate 45 such as in inlet 30
The spiral drain piece extended between liquid outlet 31, the cooling water entered from inlet 30 in cooling chamber 32 will be in deflection plate 45
In the presence of without the fluid interchange of dead angle ground, and flowed out from liquid outlet 31.
The preferred embodiment of the present invention is described in detail above in association with accompanying drawing, still, the present invention is not limited to above-mentioned reality
The detail in mode is applied, in the range of the technology design of the present invention, a variety of letters can be carried out to technical scheme
Monotropic type, these simple variants belong to protection scope of the present invention.
It is further to note that each particular technique feature described in above-mentioned embodiment, in not lance
In the case of shield, can be combined by any suitable means, in order to avoid unnecessary repetition, the present invention to it is various can
The combination of energy no longer separately illustrates.
In addition, various embodiments of the present invention can be combined randomly, as long as it is without prejudice to originally
The thought of invention, it should equally be considered as content disclosed in this invention.
Claims (10)
1. a kind of vertical condensation device, it is characterised in that including：
Liquid storage cylinder (28) is formed with drain pan (27), the drain pan (27)；
Air inlet vertical condensation cylinder (29) and outlet vertical condensation cylinder (34), the air inlet vertical condensation cylinder (29) and the outlet are vertical
Formula condensation tube (34) is vertically arranged on the upper shell wall of the drain pan (27) respectively, and the air inlet vertical condensation cylinder (29) includes tool
There are the inlet chamber (42) of air inlet and the cooling chamber (32) with inlet (30) Yu liquid outlet (31), the outlet vertical condensation
Cylinder (34) includes the outlet chamber (43) with gas outlet and the cooling chamber (32) with inlet (30) Yu liquid outlet (31), its
In,
It is respectively separated and erects in the cooling chamber (32) of the air inlet vertical condensation cylinder (29) and outlet vertical condensation cylinder (34)
Many tracheaes (33) are directly provided with, wherein,
The upper end of many tracheaes (33) in air inlet vertical condensation cylinder (29) connected with the inlet chamber (42) and
Lower end is connected with the liquid storage cylinder (28),
The upper end of many tracheaes (33) in outlet vertical condensation cylinder (34) connected with the outlet chamber (43) and
Lower end is connected with the liquid storage cylinder (28).
2. vertical condensation device according to claim 1, it is characterised in that be provided with least one described tracheae (33)
The spiral guide sheet (35) extended along the axial direction of pipe, to form the passage extended spirally in the tracheae (33).
3. vertical condensation device according to claim 2, it is characterised in that the thickness of the spiral guide sheet (35) is 1mm-
3mm。
4. vertical condensation device according to claim 1, it is characterised in that be provided with dividing plate in the drain pan (27)
(36), the liquid storage cylinder (28) is divided into upper chambers (37) and lower chamber (38) by the dividing plate (36), wherein, the air inlet is stood
The lower end of many tracheaes (33) in formula condensation tube (29) is connected with the upper chambers (37), the outlet vertical condensation cylinder
(34) lower end of many tracheaes (33) in is connected with the upper chambers (37), and the upper chambers (37) and it is described under
Switch valve (39) is provided between portion's chamber (38).
5. vertical condensation device according to claim 4, it is characterised in that the dividing plate (36) is towards the switch valve
(39) it is in tilted layout.
6. vertical condensation device according to claim 4, it is characterised in that the top of the lower chamber (38) is provided with row
Air valve, and the bottommost of the lower chamber (38) is provided with control valve (46).
7. vertical condensation device according to claim 1, it is characterised in that in the liquid storage cylinder (28), the liquid storage
It is provided with the upper shell wall of chamber (28) between air inlet vertical condensation cylinder (29) and outlet vertical condensation cylinder (34)
Flow-stopping plate (44), wherein,
The lower end of many tracheaes (33) in the air inlet vertical condensation cylinder (29) and outlet vertical condensation cylinder (34)
Air guide is formed between the chamber and the lower edge of the flow-stopping plate (44) that are connected between the lower end of many interior tracheaes (33)
Interval.
8. vertical condensation device according to claim 7, it is characterised in that the flow-stopping plate (44) is multiple, and edge
Gas flow direction, the height of the flow-stopping plate (44) of upstream is more than the height of the flow-stopping plate (44) in downstream.
9. vertical condensation device according to claim 1, it is characterised in that the air inlet vertical condensation cylinder is (29) and described
Outlet vertical condensation cylinder (34) respective inlet (30) is located at cylinder bottom and is connected with total feed tube (40)；
The air inlet vertical condensation cylinder (29) and outlet vertical condensation cylinder (34) respective liquid outlet (31) are located on cylinder
Portion is simultaneously connected with main drain pipe (41).
10. the vertical condensation device according to any one in claim 1-9, it is characterised in that the air inlet is vertical cold
Deflection plate (45) is respectively arranged with solidifying cylinder (29) and outlet vertical condensation cylinder (34) respective cooling chamber (32).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710607915.2A CN107308676A (en) | 2017-07-24 | 2017-07-24 | Vertical condensation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710607915.2A CN107308676A (en) | 2017-07-24 | 2017-07-24 | Vertical condensation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107308676A true CN107308676A (en) | 2017-11-03 |
Family
ID=60179065
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710607915.2A Withdrawn CN107308676A (en) | 2017-07-24 | 2017-07-24 | Vertical condensation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107308676A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113827999A (en) * | 2021-10-09 | 2021-12-24 | 济南恒誉环保科技股份有限公司 | Multistage cooling and purifying device for cracked oil gas |
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| CN205360648U (en) * | 2015-11-10 | 2016-07-06 | 中山凯旋真空技术工程有限公司 | Vacuum condenser and be equipped with this vacuum condenser's vacuum flash system |
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|---|---|---|---|---|
| CN201561682U (en) * | 2009-12-04 | 2010-08-25 | 山东美陵化工设备股份有限公司 | Vertical condenser with double inclined baffle plates |
| CN102585919A (en) * | 2012-03-06 | 2012-07-18 | 宁夏三友环保设备制造有限公司 | Combined type gas dry-decoking condensing unit |
| CN103203157A (en) * | 2013-03-20 | 2013-07-17 | 杭州中环环保工程有限公司 | Dichloromethane waste gas treating method and system thereof |
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| CN205360648U (en) * | 2015-11-10 | 2016-07-06 | 中山凯旋真空技术工程有限公司 | Vacuum condenser and be equipped with this vacuum condenser's vacuum flash system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113827999A (en) * | 2021-10-09 | 2021-12-24 | 济南恒誉环保科技股份有限公司 | Multistage cooling and purifying device for cracked oil gas |
| CN113827999B (en) * | 2021-10-09 | 2022-08-30 | 济南恒誉环保科技股份有限公司 | Multistage cooling and purifying device for cracked oil gas |
| WO2022179112A1 (en) * | 2021-10-09 | 2022-09-01 | 济南恒誉环保科技股份有限公司 | Multistage cooling and purifying device for cracked oil gas |
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Application publication date: 20171103 |
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