CN206176734U - Novel conduction oil furnace system's exhaust and separation device - Google Patents
Novel conduction oil furnace system's exhaust and separation device Download PDFInfo
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- CN206176734U CN206176734U CN201621246054.7U CN201621246054U CN206176734U CN 206176734 U CN206176734 U CN 206176734U CN 201621246054 U CN201621246054 U CN 201621246054U CN 206176734 U CN206176734 U CN 206176734U
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- 238000000926 separation method Methods 0.000 title abstract description 10
- 238000003860 storage Methods 0.000 claims abstract description 15
- 239000003921 oil Substances 0.000 claims description 249
- 238000005204 segregation Methods 0.000 claims description 16
- 239000002199 base oil Substances 0.000 claims description 6
- 238000004891 communication Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 238000012545 processing Methods 0.000 abstract description 6
- 238000000746 purification Methods 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000007872 degassing Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000341 volatile oil Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model relates to a novel conduction oil furnace system's exhaust and separation device, belong to filtration purification device field, conduction oil bypass (2) are located to communicate by conduction oil outlet of still pipe (1) in current conduction oil main line (101), be connected with in conduction oil bypass (2) and follow oil -gas separation device (3) of isolating in the conduction oil with gas, it can be with gas liquefaction and classified storage's gaseous processing apparatus (4) to locate to be connected with in gas outlet (31) of oil -gas separation device (3), be connected with the B collection portion (6) that is used for collecting the A collection portion (5) of low temperature volatility conduction oil and is used for collecting moisture on gaseous processing apparatus (4). Adopt above -mentioned structure, can go out the mixed -gas separation in the conduction oil on the basis that does not influence conduction oil main line (101) to do the categorised collection, the practicality is strong, and economic benefits is high.
Description
Technical field
This utility model belongs to filtering and purifying field, the aerofluxuss of more particularly to a kind of novel heat-conducting oil oven system and point
From device.
Background technology
Conduction oil is a kind of organic media for transmitting heat, and it has the performance of heat resistanceheat resistant cracking and chemical oxidation, is passed
The thermal efficiency is good, and rapid heat dissipation, heat stability is fine.Conduction oil has the characteristics that as industry oil heat transfer medium：In almost normal pressure
Under conditions of, it is possible to obtain very high operation temperature.The operating pressure and safety that high-temperature heating system can be substantially reduced will
Ask, improve the reliability of system and equipment；Different temperatures heating, the technique of cooling can be met within the scope of wider temperature
Demand, or realize the technological requirement of high-temperature heating and sub-cooled simultaneously with same conduction oil in same system, you can
To reduce the complexity of system and operation；Eliminate water treatment system and equipment, improve system thermal efficiency, reduce equipment and
The maintenance workload of pipeline, you can to reduce the initial cost and operating cost of heating system.Based on above-mentioned advantage, conduction oil is in recent years
To be widely used in the various occasions for needing to transmit heat, and its purposes and consumption are more and more.
When heat is transmitted using conduction oil, need to manufacture and design a set of pipeline for conduction oil transmission.Due to
Conduction oil is a kind of liquid, wherein moisture must be contained, and during heating, inherently produces vapor and volatility
Bigger oil vapour, above-mentioned vapor and oil vapour can cause some parts in pipeline when circulating in thermal conductive oil pipeline
The damage of (such as circulating pump), therefore in the prior art, it will usually arranging a device is used for vapor and oil vapour from conjunction
Separate in lattice conduction oil, with the quality of conduction oil in raising system, to improve heat transference efficiency, and protect pipeline system
Parts thereof in system.
In the prior art, generally using a kind of device for being named as expansion drum is used for above-mentioned vapor and oil vapour
Temporarily contain, with will above-mentioned mixed gas be passed through in holding vessel, when in holding vessel, due to oil and the density of water
Difference, Gu Shui is generally in the bottom of holding vessel, and one layer of oil of surface attachment of water is existing for the liquid in above-mentioned holding vessel
In technology would generally by the water conservancy in holding vessel with manually excluding, and oil therein then can be added to by filling pump it is qualified
It is continuing with conduction oil, so as to Energy Saving, reduces cost input will not waste of resource.
Not only contain qualified conduction oil yet with oil the inside obtained from above-mentioned Jing evaporations, and containing low temperature volatilization
Property unqualified conduction oil, it is added in the lump qualified conduction oil the inside can cause the pollution of conduction oil, and above-mentioned remove
Steam and except oil gas during need again by above-mentioned low temperature volatile oil distill, this process is gone round and begun again,
The load capacity of degassing apparatus is not only increased, while also result in unnecessary economic attrition.And low temperature fugitive constituent is in oil circuit
In system, once leakage can burn immediately, system unsafe factor is increased.
Utility model content
This utility model provides a kind of aerofluxuss of novel heat-conducting oil oven system and segregation apparatuss, by leading in the prior art
A conduction oil bypass is connected at the heat-conducting oil furnace outlet of deep fat main line, Oil-gas Separation dress is set again in conduction oil bypass
Put, oil vapour and vapor are separated from conduction oil so that low temperature volatilization is gradually decreased inside qualified conduction oil
Property oil and moisture, such that it is able to realize further improving the purpose of conduction oil purity, and then the load of degassing apparatus can be reduced
Amount, and economic attrition is reduced, practicality of the present utility model is improved, while improving security of system.
This utility model is achieved through the following technical solutions：A kind of aerofluxuss of novel heat-conducting oil oven system and segregation apparatuss,
Including conduction oil main line, the conduction oil main line includes heat-conducting oil furnace outlet, connects at the heat-conducting oil furnace outlet
Conduction oil bypass is provided with, the conduction oil bypass is provided with gas and oil separating plant, the bottom of the gas and oil separating plant
Oil-out is provided with, also including connection oil-out and the return line of conduction oil main line, the top of gas and oil separating plant is arranged
There is gas outlet, the gas and oil separating plant is arranged on the position higher than conduction oil main line.
Further, in order to preferably realize this utility model, also including gas treatment equipment, the gas treatment equipment
Connected with the gas and oil separating plant by the gas outlet.
Further, in order to preferably realize this utility model, the gas treatment equipment is condenser, the condenser
Including upper and lower, top is provided with and communicated with the A collection portions for collecting low temperature volatile conduction oil, and bottom is provided with and communicated with
For collecting the B collection portions of moisture.
Further, in order to preferably realize this utility model, also including A flanges and B flanges, the A collection portions pass through A
Flange is connected with gas treatment equipment, and the B collection portions are connected by B flanges with gas treatment equipment.
Further, in order to preferably realize this utility model, heat user is also included in the conduction oil main line, heat is used
The oil-in at family is connected by heat-conducting oil furnace outlet with organic heat carrier oil oven, and the oil-out of heat user is provided with and communicated with oil gas
Separator, the bottom of the gs-oil separator connects with the oil-in of oil circulating pump, the oil-out of the oil circulating pump with it is organic
The oil return opening connection of heat carrier oil oven；The conduction oil main line also includes expansion oil circuit, and the top of the gs-oil separator leads to
Cross expansion oil communication and be provided with surge tank, also including expansion drum, the oil-out of the surge tank connects with the oil-in of expansion drum
Logical, another oil-in and the expansion oil communication of expansion drum, the oil-out of the expansion drum is connected with the oil-in of oil storage tank,
The oil-out of the oil storage tank is connected by filling pump with the oil-in that surge tank is communicated with expansion drum；The return line with
Expansion oil communication；The position of the gas and oil separating plant is higher than the position of oil storage tank.
Further, in order to preferably realize this utility model, the gas and oil separating plant is deaerator.
Further, in order to preferably realize this utility model, the deaerator is centrifugal degasser.
Further, in order to preferably realize this utility model, deaerator is sent to be vacuum degasser.
Further, in order to preferably realize this utility model, the A flanges and B flanges are made by stainless steel material.
Further, in order to preferably realize this utility model, the A flanges and B flanges are made by carbon steel material.
This utility model compared with prior art, with advantages below and beneficial effect：
(1) this utility model is further improved, in conduction oil in the prior art on the basis of thermal conductive oil pipeline system
Conduction oil bypass is added in outlet of still pipeline, and is connected with for by the gas evaporated from conduction oil in conduction oil bypass
Body, including vapor and oil vapour, the gas and oil separating plant separated from liquid thermal conductivity oil, at gas and oil separating plant
Liquid thermal conductivity oil after reason reenters main line by return line, circulation is formed, so that low temperature in prior art
Volatility conduction oil and moisture gradually from qualified conduction oil the inside separate, and the gas isolated do not enter back into it is qualified
Heat-conducting oil system, so that the conduction oil purity of main system gradually rises, and then can reduce the load capacity of degassing apparatus, and
Economic attrition is reduced, practicality of the present utility model is improved；
(2) this utility model is communicated with the gas outlet of gas and oil separating plant and can cool down vapor and oil vapour
Pipeline, and be connected with condenser in the duct, for by the moisture after cooling liquid in pipeline and low temperature volatile oil temporarily
Storage, prevents it from leaking and causes environmental pollution, strengthens practicality of the present utility model；
(3) also include the A collection portions and B collection portions being connected on condenser in this utility model, be respectively used to collect low
Warm volatility conduction oil and water, using said structure, can separate the conduction oil after liquefaction with moisture, so as to recovery of classifying, enter
And strengthen practicality of the present utility model；
(4) A flanges are connected between above-mentioned condenser and A collection portions in this utility model, in condenser and B collection portions
Between be connected with B flanges, user need to operate flange when categorised collection conduction oil and moisture, only so that
Operation of the present utility model is more facilitated, and then strengthens practicality of the present utility model.
Description of the drawings
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise for not paying creative work
Under, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of embodiment 1 in this utility model；
Fig. 3 is the structural representation of embodiment 2 in this utility model；
Fig. 4 is the structural representation of embodiment 3 in this utility model；
Fig. 5 is the main structure diagram of deaerator in this utility model；
Fig. 6 is the overlooking the structure diagram of deaerator in this utility model；
Fig. 7 is the main structure diagram of condenser in this utility model；
Fig. 8 is the overlooking the structure diagram of condenser in this utility model.
1- heat-conducting oil furnaces outlet in figure；2- conduction oils are bypassed；3- gas and oil separating plants；4- gas treatment equipments；5-A is received
Collection portion；6-B collection portions；7-A flanges；8-B flanges；9- oil storage tanks；31- gas outlets；32- oil-outs；101- conduction oils are responsible for
Road；102- return lines.
Specific embodiment
To make the purpose of this utility model, technical scheme and advantage clearer, below will be to technology of the present utility model
Scheme is described in detail.Obviously, described embodiment is only a part of embodiment of this utility model, rather than all
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not before creative work is made
Resulting all other embodiment is put, the scope that this utility model is protected is belonged to.
Embodiment 1：
In the present embodiment, as shown in Fig. 2, Fig. 5, Fig. 6, a kind of aerofluxuss of novel heat-conducting oil oven system and segregation apparatuss, bag
Conduction oil main line 101 is included, the conduction oil main line 101 includes heat-conducting oil furnace outlet 1, at heat-conducting oil furnace outlet 1
Conduction oil bypass 2 is communicated with, gas and oil separating plant 3 is communicated with the conduction oil bypass 2, under the gas and oil separating plant 3
Portion connects with conduction oil main line 101, and the top of gas and oil separating plant 3 is provided with gas outlet 31.
Used as the specific embodiment of the present embodiment, the porch of above-mentioned conduction oil bypass 2 is by adpting flange and heat conduction
The heat-conducting oil furnace outlet 1 of oily main line 101 connects, in order to installing/dismounting, in the present embodiment, and above-mentioned heat-conducting oil furnace outlet
1 from threeway pipe connector or four-way pipe connector.When it is Three-way pipeline joint, respectively in three connecting tubes
Can be by the heat-conducting oil furnace of heat-conducting oil heating, conduction oil main line 101, conduction oil bypass 2 by adpting flange connection at mouthful；When
When it is four-way pipe connector, respectively can be by conduction oil by adpting flange connection at three connection mouths of pipe wherein
The heat-conducting oil furnace of heating, conduction oil main line 101, conduction oil bypass 2, the surplus next connection mouth of pipe can connect monitoring conduction oil stream
The supervising device of the information such as amount, pressure, temperature.
Because the working environment ordinary circumstance of conduction oil is 200-400 degree Celsius, more than the boiling point of moisture, therefore conduction oil exists
When heating, moisture therein will be vaporizated into vapor, and a part of low temperature volatile oil body in conduction oil also can be with
The rising of heat conduction oil temperature and be vaporizated into oil vapour.When using this utility model, connect at heat-conducting oil furnace outlet 1
Conduction oil bypass 2, the above-mentioned conduction oil with oil vapour and vapor becomes can simultaneously enter conduction oil main line 101 and conduction oil
Bypass 2.Gas and oil separating plant 3 is connected with conduction oil bypass 2, conduction oil is entered after conduction oil bypass 2, will be circulated to oil gas
Segregation apparatuss 3 carry out Oil-gas Separation.Because generally, the proportion of conduction oil is more great than the ratio of vapor and oil vapour, therefore
After the process of gas and oil separating plant 3, the gas in conduction oil is isolated from liquid heat conductive oil, and gas is filled positioned at Oil-gas Separation
3 top is put, and is discharged by being arranged on the gas outlet 31 on the top of gas and oil separating plant 3, reach the effect of purification conduction oil,
Make its purity higher, and the degasification load capacity of conduction oil main line 101 in prior art can be reduced, save Financial cost, on
The liquid heat conductive oil level after the process of gas and oil separating plant 3 is stated in the bottom of gas and oil separating plant 3, and is led by being connected to
Oil pipe continues cycling through work into conduction oil main line 101.
Used as the preferred forms of the present embodiment, above-mentioned gas and oil separating plant 3 is from centrifugal degasser or vacuum
Deaerator, to improve oil-gas separation efficiency, strengthens practicality of the present utility model.
As the preferred forms of the present embodiment, oil inlet end and the gas and oil separating plant 3 of above-mentioned gas and oil separating plant 3
There is inclination angle between the wall of side, so that conduction oil is entered inside gas and oil separating plant 3.
Used as the specific embodiment of the present embodiment, above-mentioned gas and oil separating plant 3 is arranged on compared to conduction oil main line
The higher position of oil storage tank 9 in 101.
Embodiment 2：
The present embodiment is further improved on the basis of embodiment 1, in the present embodiment, as shown in figure 3, in above-mentioned gas
Export and be connected with 31 gas treatment equipment 4, for processing the mixed gas separated from gas and oil separating plant 3.As
The specific embodiment of the present embodiment, above-mentioned gas processing meanss 4 are condenser.Mixed gas enter gas from gas outlet 31
During body processing meanss 4, due to heat preservation component, therefore mixed gas are not provided with the pipe side wall that it connects in pipeline
To gradually cool down during interior flowing and be changed into liquid, not yet be cooled to the mixed gas of liquid further cold in condenser
But liquefaction is liquid.
In the present embodiment, above-mentioned gas processing meanss 4 are arranged on the position lower compared to gas and oil separating plant 3, therefore become
Water and low temperature volatile oily automatically flowing in self gravitation decline into liquid is temporarily preserved in gas treatment equipment 4.
As another embodiment of the present embodiment, above-mentioned for connecting gas outlet 31 and gas treatment equipment
Cooling-part can be set on 4 pipeline lateral wall, to the temperature for reducing wherein mixed gas, accelerate the process of its liquefaction,
Improve efficiency.
Embodiment 3：
The present embodiment is further qualified on the basis of embodiment 2, in this enforcement, as shown in figure 4, above-mentioned condenser is in
Can-like, the above-mentioned pipeline connected with gas outlet 31 passes through the upper surface of condenser, and connects with condenser inside, in condenser
Top be communicated with A collection portions 5, be communicated with B collection portions 6 in its underpart.
Into the moisture after condenser with low temperature volatile conduction oil because proportion is different, therefore layering point can automatically occur
From.Moisture will be located at the bottom of condenser than great；Conduction oil is smaller, by positioned at the top of condenser.User is available
A collection portions 5 collect the moisture in condenser, and using B collection portions 6 the low temperature volatile conduction oil in condenser is collected, so as to incite somebody to action
Conduction oil in condenser no longer enters with moisture classification recycling, the low temperature volatile conduction oil collected wherein in B collection portions 6
Enter conduction oil main line 101, reach the effect of conduction oil in purification main line.
Embodiment 4：
The present embodiment is further improved on the basis of embodiment 3, in the present embodiment, as shown in Figure 7, Figure 8, above-mentioned A
Collection portion 5 is connected by A flanges 7 with the top of condenser, and B collection portions 6 are connected by B flanges 8 with the bottom of condenser, are used
Person only need to operate A flanges 7 and B flanges 8 when collection work is operated, simple and convenient.As the concrete of the present embodiment
Embodiment, above-mentioned A flanges 7 and B flanges 8 are made up of stainless steel material or carbon steel material.
As another embodiment of the present embodiment, can select valve and replace above-mentioned flange to play connection effect, and
And the controllability of valve is higher.Used as the specific embodiment of the present embodiment, above-mentioned valve can select electromagnetic valve or manual
Valve.
Embodiment 5：
The present embodiment is further improved on the basis of above-described embodiment, in the present embodiment, above-mentioned conduction oil bypass 2
Quantity is more than 1, to improve degassing efficiency.
Embodiment 6：
The present embodiment is further qualified on the basis of above-described embodiment, in the present embodiment, as shown in figure 1, above-mentioned use
It is in downward-sloping state arrangement in gas outlet 31 is connected with the pipeline of gas treatment equipment 4, to facilitate mixed gas in liquid
After change in the presence of its own gravity, inflow gas segregation apparatuss 4.
Embodiment 7：
The present embodiment is described further on the basis of above-described embodiment, in the present embodiment, as shown in figure 1, above-mentioned lead
Also include heat user in deep fat main line 101, the oil-in of heat user is by heat-conducting oil furnace outlet 1 and organic heat carrier oil oven
Connection, the oil-out of heat user is provided with and communicated with gs-oil separator, for by the conduction oil for circulating out from heat user
Gas is separated from conduction oil, including oil vapour and vapor.Due to conduction oil it is different from the proportion of mixed gas,
Therefore in gs-oil separator, conduction oil will be located at top positioned at bottom, mixed gas, arrange in the bottom connection of gs-oil separator
There is oil circulating pump, for the conduction oil in gs-oil separator to be drawn back into organic heat carrier oil circuit again, form circulation.
The conduction oil main line 101 also includes that connection is used for by part conduction oil and mixing on gs-oil separator top
The expansion oil circuit of gas, above-mentioned expansion oil circuit is respectively communicated with the oil-in of surge tank and expansion drum, due to from Oil-gas Separation
The gas and part conduction oil separated in device is respectively provided with higher temperature, therefore it is passed directly into expansion drum, is easily caused swollen
The oxidation of swell and damage, therefore above-mentioned expansion oil circuit connect first be surge tank oil-in, on this basis, then will expansion
Oil circuit is connected at the oil-in of expansion drum, and the oil-out of surge tank is connected with another oil-in of expansion drum,
Realize that the part conduction oil from gs-oil separator out initially enters surge tank in this way, after cooling down in surge tank, then
Into expansion drum.Expansion oil circuit is also connected to an oil-in of expansion drum simultaneously, when pressure is excessive in conduction oil main line
When, part conduction oil and mixed gas circulate not in time from surge tank, can be directly oily by the expansion being connected on expansion drum
Road enters expansion drum, reaches the purpose of pressure release.
The oil-in connection of the oil-out oil storage tank of above-mentioned expansion drum, the conduction oil after cooling down in expansion drum flows into oil storage
Tank；Filling pump is provided with and communicated between the oil-out of oil storage tank and the oil-in of expansion drum, when leading in conduction oil main line
When deep fat pressure is inadequate, user can pass through filling pump by oil storage tank conduction oil filling heat-conductive oil main line, so as to
Ensure the pressure in conduction oil main line.
Above-mentioned return line 102 and expansion pipeline connection, the conduction oil injection expansion tube flowed out from return line 102
Road, then via the above-mentioned process of circulation, realize the effect circulated in conduction oil main line.
Embodiment 8：
The present embodiment is described further on the basis of above-described embodiment, in the present embodiment, as shown in figure 1, above-mentioned storage
Oil tank 9 includes graviation tank and low level oil tank, and above-mentioned gas and oil separating plant 3 is arranged on the position higher than graviation tank.
Using the principle of physics in graviation tank, mixed gas are layered from conduction oil and are isolated；Moisture therein
Enter low level oil tank with conduction oil, user can the mode of manually draining water is separated from low level oil tank.
The above, specific embodiment only of the present utility model, but protection domain of the present utility model do not limit to
In this, any those familiar with the art can readily occur in change in the technical scope that this utility model is disclosed
Or replace, all should cover within protection domain of the present utility model.Therefore, protection domain of the present utility model should be with the power
The protection domain that profit is required is defined.
Claims (10)
1. a kind of aerofluxuss of novel heat-conducting oil oven system and segregation apparatuss, it is characterised in that：Including conduction oil main line (101),
The conduction oil main line (101) includes heat-conducting oil furnace outlet (1), and heat-conducting oil furnace outlet (1) place is provided with and communicated with
Conduction oil bypasses (2), and conduction oil bypass (2) is provided with and communicated with gas and oil separating plant (3), the gas and oil separating plant (3)
Bottom be provided with oil-out (32), also including the return line of connection oil-out (32) and conduction oil main line (101)
(102), the top of gas and oil separating plant (3) is provided with gas outlet (31), and the gas and oil separating plant (3) is installed in than heat conduction
The high position of oily main line (101).
2. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 1 and segregation apparatuss, it is characterised in that：Also wrap
Gas treatment equipment (4) is included, the gas treatment equipment (4) is by the gas outlet (31) and the gas and oil separating plant
(3) connect.
3. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 2 and segregation apparatuss, it is characterised in that：It is described
Gas treatment equipment (4) is condenser, and the condenser includes upper and lower, and top is provided with and communicated with waves for collecting low temperature
The A collection portions (5) of the property sent out conduction oil, bottom is provided with and communicated with the B collection portions (6) for collecting moisture.
4. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 3 and segregation apparatuss, it is characterised in that：Also wrap
A flanges (7) and B flanges (8) are included, the A collection portions (5) are connected by A flanges (7) with gas treatment equipment (4), the B is received
Collection portion (6) is connected by B flanges (8) with gas treatment equipment (4).
5. a kind of aerofluxuss of the novel heat-conducting oil oven system according to any one of claim 1-4 and segregation apparatuss, it is special
Levy and be：Also include heat user in the conduction oil main line (101), the oil-in of heat user passes through heat-conducting oil furnace outlet
(1) connect with organic heat carrier oil oven, the oil-out of heat user is provided with and communicated with gs-oil separator, under the gs-oil separator
Portion connects with the oil-in of oil circulating pump, and the oil-out of the oil circulating pump is connected with the oil return opening of organic heat carrier oil oven；Institute
Stating conduction oil main line (101) also includes expansion oil circuit, and the top of the gs-oil separator is provided with by expanding oil communication
Surge tank, also including expansion drum, the oil-out of the surge tank is connected with the oil-in of expansion drum, another oil-feed of expansion drum
Mouth is connected with expansion oil communication, the oil-out of the expansion drum with the oil-in of oil storage tank, and the oil-out of the oil storage tank leads to
Cross filling pump and connect with the oil-in that surge tank is communicated with expansion drum；The return line (102) and expansion oil communication；Institute
The position for stating gas and oil separating plant (3) is higher than the position of oil storage tank (9).
6. a kind of aerofluxuss of the novel heat-conducting oil oven system according to any one of claim 1-4 and segregation apparatuss, it is special
Levy and be：The gas and oil separating plant (3) is deaerator.
7. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 6 and segregation apparatuss, it is characterised in that：It is described
Deaerator is centrifugal degasser.
8. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 6 and segregation apparatuss, it is characterised in that：It is described
Deaerator is vacuum degasser.
9. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 4 and segregation apparatuss, it is characterised in that：It is described
A flanges (7) and B flanges (8) are made by stainless steel material.
10. a kind of aerofluxuss of novel heat-conducting oil oven system according to claim 4 and segregation apparatuss, it is characterised in that：Institute
State A flanges (7) and B flanges (8) are made by carbon steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621246054.7U CN206176734U (en) | 2016-11-16 | 2016-11-16 | Novel conduction oil furnace system's exhaust and separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621246054.7U CN206176734U (en) | 2016-11-16 | 2016-11-16 | Novel conduction oil furnace system's exhaust and separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206176734U true CN206176734U (en) | 2017-05-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621246054.7U Expired - Fee Related CN206176734U (en) | 2016-11-16 | 2016-11-16 | Novel conduction oil furnace system's exhaust and separation device |
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| CN (1) | CN206176734U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108103890A (en) * | 2017-12-15 | 2018-06-01 | 佛山高富中石油燃料沥青有限责任公司 | A kind of safety and environmental protection boils the anti-bumping device of oil |
| CN108180657A (en) * | 2017-12-27 | 2018-06-19 | 武汉都市环保工程技术股份有限公司 | Heat conduction reconditioner and trough solar power generation system |
-
2016
- 2016-11-16 CN CN201621246054.7U patent/CN206176734U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108103890A (en) * | 2017-12-15 | 2018-06-01 | 佛山高富中石油燃料沥青有限责任公司 | A kind of safety and environmental protection boils the anti-bumping device of oil |
| CN108180657A (en) * | 2017-12-27 | 2018-06-19 | 武汉都市环保工程技术股份有限公司 | Heat conduction reconditioner and trough solar power generation system |
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