CN206474464U - A kind of hydrocarbon cleaning equipment - Google Patents
A kind of hydrocarbon cleaning equipment Download PDFInfo
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- CN206474464U CN206474464U CN201621270881.XU CN201621270881U CN206474464U CN 206474464 U CN206474464 U CN 206474464U CN 201621270881 U CN201621270881 U CN 201621270881U CN 206474464 U CN206474464 U CN 206474464U
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- condenser
- agent
- carbon hydrogen
- liquid
- hydrogen detergent
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Abstract
The utility model provides a kind of hydrocarbon cleaning equipment, including purging system, first cooling system, the second cooling system, first Distallation systm, after-fractionating system and drying system, purging system includes rinse bath, first cooling system includes the first condenser and is looped around the first condenser coil of the first condenser surface, first Distallation systm includes the first alembic, first alembic is provided with first entrance and first outlet, the second cooling system includes the second condenser and is looped around the second condenser coil of the second condenser surface, after-fractionating system includes after-fractionating tank, after-fractionating tank is provided with second outlet and second entrance, drying system includes dry slot, the spray thrower being located at the top of dry slot and the collection port for being located at dry trench bottom, agent for carbon hydrogen detergent dirty liquid in first condenser coil is used to cool down the first steam in the first condenser, agent for carbon hydrogen detergent dirty liquid in second condenser is used to cool down the liquid in the second condenser coil, the equipment takes full advantage of recovery heat.
Description
Technical field
The utility model is related to industry cleaning link field, and in particular to a kind of hydrocarbon cleaning equipment.
Background technology
In industry cleaning link industry, many techniques can be applied to hydrocarbon cleaning technology, hydrocarbon cleaning equipment and cleaning process
Also it is widely known by the people.As Chinese patent CN104056810A discloses a kind of hydrocarbon cleaning machine with explosion prevention function, including cleaning
Groove, has ultrasonic wave shake plate in the rinse bath, is taken out the hydrocarbon gas volatilized in ultrasonic cleaner with pump-line, clearly
Except the hydrocarbon vapor produced in cleaning process, explosion danger is reduced.Chinese patent CN205351959U discloses one kind
The drying equipment of agent for carbon hydrogen detergent, including drying box and for the explosion-proof fan towards air blast in drying box, drying box and blasting-proof machine
Between be provided with check-valves, improve drying process security.Chinese patent CN202356344U discloses a kind of hydrocarbon cleaning and set
System is washed in standby steam bath, includes wash chamber and steam generator, high using being produced under high vacuum to high-temp liquid heating
The mode of warm steam, quantity of steam is big, steam pressure is high, and cleaning performance is more preferable, it is possible to decrease energy consumption and reduction potential safety hazard.It is Chinese special
Sharp CN202460162U discloses a kind of distillation recovery system of hydrocarbon cleaning equipment, including heater, alembic and condensation
Recover, the distillation recovery system makes alembic keep condition of high vacuum degree using vavuum pump, it is possible to increase distillation efficiency.
Traditional industry cleaning link common practices is that hydrocarbon solution is contained in rinse bath, passes through workpiece, material strip described
Cleaned when rinse bath, and one hot-air seasoning groove is set in the back segment of rinse bath, make workpiece or material strip by described
Drying is washed away by hot blast during hot-air seasoning groove, prevents from taking out of cleaning fluid, is also convenient for putting into the processing of next stage immediately and uses.
But at present using in hydrocarbon cleaning technology, the energy consumption of generation is higher, and most heat is difficult to be recycled.It is therefore desirable to
New hydrocarbon cleaning equipment is provided, to improve the heat utilization ratio of agent for carbon hydrogen detergent cleaning process.
Utility model content
To solve the above problems, the utility model provides a kind of hydrocarbon cleaning equipment, the hydrocarbon cleaning equipment can be right
Agent for carbon hydrogen detergent carries out energy-conservation recovery, improves the utilization ratio of heat.
The utility model provides a kind of hydrocarbon cleaning equipment, including purging system, the first cooling system, the second cooling system
System, the first Distallation systm, after-fractionating system and drying system, the purging system include rinse bath, first cooling system
System includes the first condenser and is looped around the first condenser coil of first condenser surface, and first Distallation systm includes
First alembic, first alembic be provided with first entrance and first outlet, one end of first condenser coil with it is described
Rinse bath is connected to the agent for carbon hydrogen detergent dirty liquid in rinse bath being persistently delivered in first condenser coil, other end
It is connected to the agent for carbon hydrogen detergent dirty liquid in first condenser coil being delivered to first distillation with the first entrance
Heating distillation is carried out in tank, the first outlet is connected to heat agent for carbon hydrogen detergent dirty liquid with first condenser distills
First steam of output is delivered in first condenser, and the agent for carbon hydrogen detergent dirty liquid in first condenser coil is used for cold
The first steam in first condenser, obtains the new liquid of the first agent for carbon hydrogen detergent；
The second cooling system includes the second condenser and is looped around the second condensate pans of second condenser surface
Pipe, the after-fractionating system includes after-fractionating tank, and the after-fractionating tank is provided with second outlet and second entrance, described dry
Drying system includes dry slot, the spray thrower being located at the top of dry slot and the collection port for being located at dry trench bottom, second condensation
One end of device is connected to the agent for carbon hydrogen detergent dirty liquid in the rinse bath being persistently delivered to described second with the rinse bath
In condenser, the other end and the second entrance of second condenser are connected to will be hydrocarbon in second condenser
Cleaning agent dirty liquid is delivered to progress heating distillation in after-fractionating tank, and the second outlet is connected with the spray thrower, made hydrocarbon
Second steam of cleaning agent dirty liquid heating distillation output is sprayed in the dry slot by the spray thrower to be used to dry workpiece,
The collection port is used to collecting second steam liquid of condensed formation and to be delivered to described second cold in the drying process
In solidifying coil pipe, the agent for carbon hydrogen detergent dirty liquid in second condenser is used to cool down the liquid in second condenser coil
Body, obtains the new liquid of the second agent for carbon hydrogen detergent.
Preferably, first cooling system also includes the 3rd condenser coil for being looped around first condenser surface,
Cooling water is connected with 3rd condensate pans.
Preferably, the hydrocarbon cleaning equipment also includes the 3rd cooling system, and the 3rd cooling system enters for described in
One step cools down the new liquid of the second agent for carbon hydrogen detergent of the second condenser coil output.
Preferably, the 3rd cooling system includes the 3rd condenser and is looped around the 4th of the 3rd condenser surface
Condenser coil, the new liquid of the second agent for carbon hydrogen detergent of second condenser coil output enters in the 3rd condenser, and described the
Cooling water is connected with four condenser coils to be used to further cool down the new liquid of the second agent for carbon hydrogen detergent in the 3rd condenser.
Preferably, the bottom of rinse bath goes out provided with the outlet of the first agent for carbon hydrogen detergent dirty liquid and the second agent for carbon hydrogen detergent dirty liquid
Mouthful, the first agent for carbon hydrogen detergent dirty liquid outlet is connected with first condenser coil, and the second agent for carbon hydrogen detergent dirty liquid goes out
Mouth is connected with second condenser.
Preferably, the purging system includes the first rinse bath and the second rinse bath, first rinse bath and described the
One condenser coil is connected, and second rinse bath is connected with second condenser.
Preferably, the hydrocarbon cleaning equipment is additionally provided with new liquid bath, and the new liquid bath is hydrocarbon clear for storing described first
The new liquid of lotion and/or the new liquid of the second agent for carbon hydrogen detergent, the new liquid bath are connected with the rinse bath by automatic valve.
Preferably, tank level control system is provided with the rinse bath, when the liquid level of the rinse bath is less than target level,
The new liquid of the first agent for carbon hydrogen detergent and/or the new liquid of the second agent for carbon hydrogen detergent in the new liquid bath are entered by automatic valve
It is used for cleaning workpiece in the rinse bath.
Preferably, first Distallation systm also includes first heater, and the first heater, which is used to heat, to be steamed
Evaporate the agent for carbon hydrogen detergent dirty liquid in first alembic；The after-fractionating system also includes secondary heating mechanism, described the
Two heaters are used to heat the agent for carbon hydrogen detergent dirty liquid in the distillation after-fractionating tank.
What the utility model was provided saves recyclable hydrocarbon cleaning equipment, can both enable agent for carbon hydrogen detergent effective
Reclaim, recovery heat is taken full advantage of again to keep cleaning and recovered temperature；Both saved and required heat is heated in alembic
Amount, has saved the consumption of cooling water again.
To sum up, the utility model beneficial effect includes the following aspects：
What the 1st, the utility model was provided saves recyclable hydrocarbon cleaning equipment, both agent for carbon hydrogen detergent can be had
Effect is reclaimed, and recovery heat is taken full advantage of again to keep cleaning and recovered temperature；Both saved required for being heated in alembic
Heat, has saved the consumption of cooling water again；
Brief description of the drawings
A kind of structural representation for hydrocarbon cleaning equipment that Fig. 1 provides for the embodiment of the utility model one.
Embodiment
As described below is preferred embodiment of the present utility model, it is noted that for the ordinary skill of the art
For personnel, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these improve and moistened
Decorations are also considered as protection domain of the present utility model.
The structural representation for a kind of hydrocarbon cleaning equipment that Fig. 1 provides for the embodiment of the utility model one, such as Fig. 1 institutes
Show, the utility model provides a kind of hydrocarbon cleaning equipment, including purging system 1, the first cooling system 2, the second cooling system
5th, the first Distallation systm 3, after-fractionating system 6 and drying system 7, purging system 1 include rinse bath, and the first cooling system 2 is wrapped
Include the first condenser 21 and be looped around first condenser coil 22 on the surface of the first condenser 21, the first 3 systems of distillation include first
Alembic 31, the first alembic 31 is provided with first entrance 311 and first outlet 312, one end of the first condenser coil 22 and cleaning
Groove is connected to the agent for carbon hydrogen detergent dirty liquid in rinse bath being persistently delivered in the first condenser coil 22, other end and first
Entrance 311 is connected to the agent for carbon hydrogen detergent dirty liquid in the first condenser coil 22 being delivered in the first alembic 31 and heated
Distillation, the condenser 21 of first outlet 312 and first is connected to heat agent for carbon hydrogen detergent dirty liquid the first steam of distillation output
It is delivered in the first condenser 21, the agent for carbon hydrogen detergent dirty liquid in the first condenser coil 22 is used to cool down in the first condenser 21
First steam, obtains the new liquid of the first agent for carbon hydrogen detergent；
The second cooling system 5 includes the second condenser 51 and is looped around second condenser coil on the surface of the second condenser 51
52, after-fractionating system 6 includes after-fractionating tank 61, and after-fractionating tank 61 is provided with second outlet 612 and second entrance 611, does
Drying system 7 includes dry slot 71, is located at the spray thrower 72 at the top of dry slot 71 and is located at the collection port 73 of dry trench bottom, second
One end of condenser 51 is connected to the agent for carbon hydrogen detergent dirty liquid in rinse bath being persistently delivered to the second condenser with rinse bath
In 51, the other end and the second entrance 611 of the second condenser 51 are connected to the agent for carbon hydrogen detergent in the second condenser 51 is dirty
Liquid is delivered to progress heating distillation in after-fractionating tank 61, and second outlet 612 is connected with spray thrower 72, makes agent for carbon hydrogen detergent dirty liquid
Second steam of heating distillation output is sprayed in dry slot 71 by spray thrower 72 to be used to dry workpiece, and collection port 73 is used to receive
Collect the second steam and the liquid of condensed formation and be delivered in the drying process in the second condenser coil 52, in the second condenser 51
Agent for carbon hydrogen detergent dirty liquid be used for cool down the second condenser coil in 52 liquid, obtain the new liquid of the second agent for carbon hydrogen detergent.
Especially it is distilled to recover with during hot-air seasoning using hydrocarbon cleaning technology at present, the energy consumption of generation is higher, greatly
Partial heat is difficult to be recycled.
The first steam in the hydrocarbon cleaning equipment that the utility model is provided, including two sets of power saving units, the first condenser
By the agent for carbon hydrogen detergent dirty liquid cooling in the first condenser coil, the liquid in the condensation that cools, the second condenser coil is by the second condensation
Agent for carbon hydrogen detergent dirty liquid cooling in device is so as to cool, while agent for carbon hydrogen detergent dirty liquid temperature is also improved, on the one hand, make
With agent for carbon hydrogen detergent dirty liquid as cooling medium, the consumption of cooling water has been saved.On the other hand, steam is taken full advantage of in drying
During condensed formation liquid heat, agent for carbon hydrogen detergent dirty liquid is preheated, agent for carbon hydrogen detergent dirty liquid temperature is put forward
Height, has saved and required heat is heated in follow-up alembic.Therefore the hydrocarbon cleaning equipment that the utility model is provided improves carbon
Hydrogen cleaning agent is distilled to recover the utilization rate with the heat in drying process.
In the utility model, bottom of rinse bath is provided with the outlet of the first agent for carbon hydrogen detergent dirty liquid and the second agent for carbon hydrogen detergent dirty liquid
Outlet, the first agent for carbon hydrogen detergent dirty liquid outlet is connected with the first condenser coil, and the second agent for carbon hydrogen detergent dirty liquid is exported and second is cold
Condenser is connected.That is the first cooling system and the second cooling system of utility model can be connected with same rinse bath.
In the utility model, purging system can include at least one rinse bath.
As shown in figure 1, in the utility model, purging system includes the first rinse bath 11 and the second rinse bath 12, and first is clear
Washing trough 11 is connected with the first condenser coil 22, and the second rinse bath 12 is connected with the second condenser 51.
In the utility model, first entrance 311 is arranged on the bottom of the first alembic.
In the utility model, first outlet 312 is arranged on the top of the first alembic.
In the utility model, the first cooling system also includes the 3rd condenser coil for being looped around the first condenser surface, the
Cooling water is connected with three condensate pans.
In the utility model, the 3rd condenser coil is arranged side by side with the first condenser coil.
For further cooling steam, the utility model is additionally provided can lead in the 3rd condenser coil, the 3rd condenser coil
Enter cooling water or be passed through other cooling mediums.
In the utility model, the first Distallation systm also includes first heater, and first heater, which is used to heat, to be distilled
Agent for carbon hydrogen detergent dirty liquid in first alembic.
In the utility model, first heater includes the first heating coil and the first heat-conducting oil pipes, the first heating coil
The inside of the first alembic is arranged on, the first heat-conducting oil pipes are arranged on the lower section of the first alembic, the first heating coil and first
Conduction oil is connected with heat-conducting oil pipes.
In the utility model, the first heating coil and the first heat-conducting oil pipes are connected with heat conduction oil groove, and heat conduction oil groove passes through
Conduction oil is delivered in the first heating coil and the first heat-conducting oil pipes by Heat-transfer Oil Pump respectively.
In the utility model, second entrance 611 is arranged on the bottom of after-fractionating tank.
In the utility model, second outlet 612 is arranged on the top of after-fractionating tank.
In the utility model, hydrocarbon cleaning equipment also includes the 3rd cooling system, and the 3rd cooling system is used for further cold
But the new liquid of the second agent for carbon hydrogen detergent that the second condenser coil is exported.
In the utility model, the 3rd cooling system includes the 3rd condenser and be looped around the 3rd condenser surface the 4th is cold
Solidifying coil pipe, the new liquid of the second agent for carbon hydrogen detergent of the second condenser coil output enters in the 3rd condenser, leads in the 4th condenser coil
Have cooling water be used for further cooling the 3rd condenser in the new liquid of the second agent for carbon hydrogen detergent.
For the further cooling new liquid of the second agent for carbon hydrogen detergent, the utility model additionally provides the 3rd cooling system, and the 4th is cold
Cooling water can be passed through in solidifying coil pipe or is passed through other cooling mediums.
In the utility model, after-fractionating system also includes secondary heating mechanism, and secondary heating mechanism, which is used to heat, to be distilled
Agent for carbon hydrogen detergent dirty liquid in after-fractionating tank.
In the utility model, secondary heating mechanism includes the second heating coil and the second heat-conducting oil pipes, the second heating coil
The inside of after-fractionating tank is arranged on, the second heat-conducting oil pipes are arranged on the lower section of after-fractionating tank, the second heating coil and second
Conduction oil is connected with heat-conducting oil pipes.
In the utility model, the second heating coil and the second heat-conducting oil pipes are connected with heat conduction oil groove, and heat conduction oil groove passes through
Conduction oil is delivered in the second heating coil and the second heat-conducting oil pipes by Heat-transfer Oil Pump respectively.
Deep fat in heat conduction oil groove is reached in heat-conducting oil pipes and heating coil to enter agent for carbon hydrogen detergent dirty liquid by Heat-transfer Oil Pump
Row heating.Heater is to the bottom of alembic and is internally heated, and two kinds of mode of heatings are combined, and heats more straight
Connect, contact area is bigger.
In the utility model, spray thrower is arranged on the top of dry slot by way of conventional.
In the utility model, the quantity of spray thrower is at least one.
In the utility model, the quantity of dry slot is at least one.Multiple sprays can be set at the top of a dry slot
Device, can also set multiple dry slots to be respectively provided with least one spray thrower at the top of each dry slot.
In the utility model, when the quantity of dry slot is multiple, each collection port for drying trench bottom collects what is obtained
It is delivered to together in the second condenser coil after liquid mixing.
In the utility model, hydrocarbon cleaning equipment is additionally provided with new liquid bath, and it is new that new liquid bath is used for the first agent for carbon hydrogen detergent of storage
Liquid and/or the new liquid of the second agent for carbon hydrogen detergent, new liquid bath are connected with rinse bath by automatic valve.
In the utility model, tank level control system is provided with rinse bath, when the liquid level of rinse bath is less than target level, newly
The new liquid of the first agent for carbon hydrogen detergent and/or the new liquid of the second agent for carbon hydrogen detergent in liquid bath are entered in rinse bath by automatic valve and used
In cleaning workpiece.
In the utility model, the new liquid of the first agent for carbon hydrogen detergent and the new liquid of the second agent for carbon hydrogen detergent can be stored in same new
In liquid bath.
In the utility model, hydrocarbon cleaning equipment is additionally provided with the first new liquid bath 42 of new liquid bath 41 and second, the first new liquid bath
41 are used to store the new liquid of the first agent for carbon hydrogen detergent, and the second new liquid bath 42 is used to store the new liquid of the second agent for carbon hydrogen detergent.
In the utility model, hydrocarbon cleaning equipment also includes what is produced in waste liquid tank, the first alembic and after-fractionating tank
Waste liquid is drained into waste liquid tank.
The steam of the utility model agent for carbon hydrogen detergent dirty liquid heating distillation output is sprayed in dry slot by spray thrower, is used
In carrying out steam clean to workpiece, the steam droplet that workpiece surface is remained after depth cleaning is by spontaneously drying, with not entering
The workpiece of row steam clean is compared, and the utility model drying time is largely shortened.So, both to have carried out depth to workpiece clear
Wash, drying time is shortened again, while taking full advantage of the heat for the high-temperature steam that distillation is produced.
In the utility model, the temperature of the first steam or the second steam is 160 DEG C -190 DEG C.
In the utility model, dry after, the second steam in the drying process the liquid of condensed formation temperature be 140
℃-150℃。
In the utility model, after heat exchange, the temperature of agent for carbon hydrogen detergent dirty liquid can reach 85 DEG C -125 DEG C.Go out from rinse bath
The temperature of the agent for carbon hydrogen detergent dirty liquid come is after 40 DEG C -45 DEG C, with the liquid heat exchange of steam or hotter, temperature can rise to 85
℃-125℃。
In the utility model, the hydrocarbon cleaning equipment provided compared to existing hydrocarbon cleaning equipment, the utility model
Heat utilization ratio can reach more than 40%.
The application process of hydrocarbon cleaning equipment that the utility model is provided is specially：
Agent for carbon hydrogen detergent dirty liquid in rinse bath is persistently delivered in the first condenser coil, then from the first condenser coil
Middle first alembic that enters carries out heating distillation, and the first steam that heating distillation is produced enters the first condensation by first outlet
Device, now, the first steam that the agent for carbon hydrogen detergent dirty liquid in the first condenser coil is used in the first cooling condenser obtain first
The new liquid of agent for carbon hydrogen detergent.Meanwhile, the agent for carbon hydrogen detergent dirty liquid in the first condenser coil is also preheated, temperature rise, subsequently
Alembic is entered back into be distilled.Whole process circulation is carried out.When the liquid level of rinse bath is less than target level, in new flow container
New liquid, which enters rinse bath, is used for cleaning workpiece；
The agent for carbon hydrogen detergent dirty liquid in rinse bath is persistently delivered in the second condenser simultaneously, then from the second condenser
Middle entrance after-fractionating tank carries out heating distillation, and the second steam that heating distillation is produced enters spray thrower by second outlet, led to
Crossing spray thrower and being sprayed in dry slot is used to dry workpiece, after drying, and collects the second steam and condenses formation in the drying process
Liquid enters in the second condenser coil, now, and the agent for carbon hydrogen detergent dirty liquid in the second condenser is used to cool down the second condenser coil
In liquid, obtain the new liquid of the second agent for carbon hydrogen detergent.Meanwhile, the agent for carbon hydrogen detergent dirty liquid in the second condenser has also obtained pre-
Heat, temperature rise, subsequently enters back into after-fractionating tank and is distilled.Whole process circulation is carried out.When the liquid level of rinse bath is less than
During target level, the new liquid in new flow container, which enters rinse bath, is used for cleaning workpiece.
What the utility model was provided saves recyclable hydrocarbon cleaning equipment, can both enable agent for carbon hydrogen detergent effective
Reclaim, recovery heat is taken full advantage of again to keep cleaning and recovered temperature；Both saved and required heat is heated in alembic
Amount, has saved the consumption of cooling water again.
The energy saving recovery method for the hydrocarbon cleaning equipment that the utility model is provided, including：
Hydrocarbon cleaning equipment as described above is provided, agent for carbon hydrogen detergent dirty liquid is persistently delivered to the first condenser coil
In, agent for carbon hydrogen detergent dirty liquid obtains the first steam after the output of the first condenser coil through the heating distillation of the first alembic, and first steams
Vapour enters by the agent for carbon hydrogen detergent dirty liquid cooling in the first condenser coil in the first condenser, and recovery obtains the first agent for carbon hydrogen detergent
New liquid；
Agent for carbon hydrogen detergent dirty liquid is persistently delivered in the second condenser, agent for carbon hydrogen detergent dirty liquid is exported from the second condenser
The second steam is obtained by the heating distillation of after-fractionating tank, the second steam is sprayed in dry slot by spray thrower is used for drying
Workpiece, dry after, collect the second steam in the drying process condensed formation liquid enter the second condenser coil in, second is cold
Liquid in solidifying coil pipe is cooled down by the agent for carbon hydrogen detergent dirty liquid in the second condenser, and recovery obtains the new liquid of the second agent for carbon hydrogen detergent.
In the utility model, by hydrocarbon cleaning while agent for carbon hydrogen detergent dirty liquid is persistently delivered in the first condenser coil
Agent dirty liquid is persistently delivered in the second condenser.
Embodiment described above only expresses several embodiments of the present utility model, and it describes more specific and detailed,
But therefore it can not be interpreted as the limitation to the utility model the scope of the claims.It should be pointed out that for the common of this area
For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to
In protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be determined by the appended claims.
Claims (9)
1. a kind of hydrocarbon cleaning equipment, it is characterised in that including purging system, the first cooling system, the second cooling system, first
Distallation systm, after-fractionating system and drying system, the purging system include rinse bath, and first cooling system includes the
One condenser and the first condenser coil for being looped around first condenser surface, first Distallation systm include the first distillation
Tank, first alembic is provided with first entrance and first outlet, and one end and the rinse bath of first condenser coil connect
Connect for the agent for carbon hydrogen detergent dirty liquid in rinse bath to be persistently delivered in first condenser coil, other end and described the
One entrance is connected to the agent for carbon hydrogen detergent dirty liquid in first condenser coil being delivered in first alembic and carried out
Heating distillation, the first outlet and first condenser are connected to heating agent for carbon hydrogen detergent dirty liquid into the of distillation output
One steam is delivered in first condenser, and the agent for carbon hydrogen detergent dirty liquid in first condenser coil is used to cool down described the
The first steam in one condenser, obtains the new liquid of the first agent for carbon hydrogen detergent；
The second cooling system includes the second condenser and is looped around the second condenser coil of second condenser surface, institute
Stating after-fractionating system includes after-fractionating tank, and the after-fractionating tank is provided with second outlet and second entrance, the dry system
System includes dry slot, the spray thrower being located at the top of dry slot and the collection port for being located at dry trench bottom, second condenser
One end is connected to the agent for carbon hydrogen detergent dirty liquid in the rinse bath being persistently delivered to second condensation with the rinse bath
In device, the other end and the second entrance of second condenser are connected to the hydrocarbon cleaning in second condenser
Agent dirty liquid is delivered to progress heating distillation in after-fractionating tank, and the second outlet is connected with the spray thrower, makes hydrocarbon cleaning
Second steam of agent dirty liquid heating distillation output is sprayed in the dry slot by the spray thrower to be used to dry workpiece, described
Collection port is used to collecting second steam liquid of condensed formation and is delivered to second condensate pans in the drying process
Agent for carbon hydrogen detergent dirty liquid in Guan Zhong, second condenser is used to cool down the liquid in second condenser coil, obtains
To the new liquid of the second agent for carbon hydrogen detergent.
2. hydrocarbon cleaning equipment as claimed in claim 1, it is characterised in that first cooling system also includes being looped around institute
State in the 3rd condenser coil of the first condenser surface, the 3rd condensate pans and be connected with cooling water.
3. hydrocarbon cleaning equipment as claimed in claim 1, it is characterised in that the hydrocarbon cleaning equipment also includes the 3rd cooling
System, the 3rd cooling system is used for the new liquid of the second agent for carbon hydrogen detergent for further cooling down the second condenser coil output.
4. hydrocarbon cleaning equipment as claimed in claim 3, it is characterised in that the 3rd cooling system includes the 3rd condenser
With the 4th condenser coil for being looped around the 3rd condenser surface, the second agent for carbon hydrogen detergent of the second condenser coil output
New liquid enters in the 3rd condenser, cooling water is connected with the 4th condenser coil cold for further cooling down the described 3rd
The new liquid of the second agent for carbon hydrogen detergent in condenser.
5. hydrocarbon cleaning equipment as claimed in claim 1, it is characterised in that the bottom of rinse bath is provided with the first hydrocarbon cleaning
Agent dirty liquid is exported and the outlet of the second agent for carbon hydrogen detergent dirty liquid, the first agent for carbon hydrogen detergent dirty liquid outlet and first condensate pans
Pipe is connected, and the second agent for carbon hydrogen detergent dirty liquid outlet is connected with second condenser.
6. hydrocarbon cleaning equipment as claimed in claim 1, it is characterised in that the purging system includes the first rinse bath and the
Two rinse baths, first rinse bath is connected with first condenser coil, second rinse bath and second condenser
Connection.
7. hydrocarbon cleaning equipment as claimed in claim 1, it is characterised in that the hydrocarbon cleaning equipment is additionally provided with new liquid bath,
The new liquid bath is used to store the new liquid of the first agent for carbon hydrogen detergent and/or the new liquid of the second agent for carbon hydrogen detergent, the new liquid
Groove is connected with the rinse bath by automatic valve.
8. hydrocarbon cleaning equipment as claimed in claim 7, it is characterised in that tank level control system is provided with the rinse bath,
When the liquid level of the rinse bath is less than target level, the new liquid of the first agent for carbon hydrogen detergent in the new liquid bath and/or described the
The new liquid of two agent for carbon hydrogen detergent is entered by automatic valve is used for cleaning workpiece in the rinse bath.
9. hydrocarbon cleaning equipment as claimed in claim 1, it is characterised in that first Distallation systm also includes the first heating
Device, the first heater is used to heat the agent for carbon hydrogen detergent dirty liquid in distillation first alembic；Described second steams
Evaporating system also includes secondary heating mechanism, and the secondary heating mechanism is used to heat hydrocarbon clear in the distillation after-fractionating tank
Lotion dirty liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621270881.XU CN206474464U (en) | 2016-11-22 | 2016-11-22 | A kind of hydrocarbon cleaning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621270881.XU CN206474464U (en) | 2016-11-22 | 2016-11-22 | A kind of hydrocarbon cleaning equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206474464U true CN206474464U (en) | 2017-09-08 |
Family
ID=59755621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621270881.XU Expired - Fee Related CN206474464U (en) | 2016-11-22 | 2016-11-22 | A kind of hydrocarbon cleaning equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206474464U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106733871A (en) * | 2016-11-22 | 2017-05-31 | 广东新球清洗科技股份有限公司 | A kind of energy saving recovery method of agent for carbon hydrogen detergent and a kind of hydrocarbon cleaning equipment |
| CN110946542A (en) * | 2018-09-26 | 2020-04-03 | 杨婇琳 | Shoe material cleaning and drying device |
-
2016
- 2016-11-22 CN CN201621270881.XU patent/CN206474464U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106733871A (en) * | 2016-11-22 | 2017-05-31 | 广东新球清洗科技股份有限公司 | A kind of energy saving recovery method of agent for carbon hydrogen detergent and a kind of hydrocarbon cleaning equipment |
| CN110946542A (en) * | 2018-09-26 | 2020-04-03 | 杨婇琳 | Shoe material cleaning and drying device |
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