CN108455693A - A kind of industrial wastes recovery and processing system and recovery and treatment method - Google Patents
A kind of industrial wastes recovery and processing system and recovery and treatment method Download PDFInfo
- Publication number
- CN108455693A CN108455693A CN201810208809.1A CN201810208809A CN108455693A CN 108455693 A CN108455693 A CN 108455693A CN 201810208809 A CN201810208809 A CN 201810208809A CN 108455693 A CN108455693 A CN 108455693A
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- main shaft
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- waste liquid
- industrial wastes
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- 239000002440 industrial waste Substances 0.000 title claims abstract description 42
- 238000011084 recovery Methods 0.000 title claims abstract description 39
- 238000012545 processing Methods 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 96
- 239000002699 waste material Substances 0.000 claims abstract description 89
- 238000004821 distillation Methods 0.000 claims abstract description 52
- 230000007246 mechanism Effects 0.000 claims abstract description 35
- 238000010438 heat treatment Methods 0.000 claims abstract description 28
- 238000007790 scraping Methods 0.000 claims description 30
- 238000003756 stirring Methods 0.000 claims description 15
- 238000012544 monitoring process Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 8
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 238000004064 recycling Methods 0.000 claims description 5
- 239000002826 coolant Substances 0.000 claims description 2
- 239000002893 slag Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 description 4
- 230000000712 assembly Effects 0.000 description 3
- 238000000429 assembly Methods 0.000 description 3
- 230000006837 decompression Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000470 constituent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 206010059410 Faecaluria Diseases 0.000 description 1
- 230000004520 agglutination Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of industrial wastes recovery and processing system and recovery and treatment methods.Industrial wastes recovery and processing system includes drain sump, condenser and waste drains pump, drain sump includes distillation still and rabbling mechanism, condenser includes steam discharge entrance, recovered liquid outlet, condensing medium inlet and condensing medium outlet, the outlet of waste drains pump connects the condensing medium inlet of condenser, and the condensing medium outlet of condenser connects the waste liquid entrance of distillation still；The exhaust vent of distillation still connects the steam discharge entrance of condenser.The industrial wastes recovery and processing system of the present invention within the condenser preheats pending waste liquid using waste liquid steam, waste liquid steam is condensed using pending waste liquid, the heat of the steam of distillation still discharge is utilized, the waste liquid entered before distillation still is preheated, the heating speed of waste liquid is fast in distillation still, and the thermal efficiency of system is high.
Description
[technical field]
The present invention relates to industrial wastes recovery processing more particularly to a kind of industrial wastes recovery and processing system and recovery processings
Method.
[background technology]
With the development of science and technology, the requirement to precise electronic, hardware and optical component surfaces processing etc. is higher and higher,
Caused consequence is that industrial wastes is more and more, and industrial wastes is the big main cause for leading to water pollution, the recycling of industrial wastes
Processing is to avoid the vital measure of pollution environment.
The utility model of Patent No. CN201020553608.4 provides a kind of decompression dehydration drying device, has：Distillation
Kettle, with stirring wing stirring distillation still inside waste rabbling mechanism, with agitating shaft drive waste rabbling mechanism stirring wing
Driving mechanism, heat distillation still inside waste heat source, make the gas evaporated from the waste inside distillation still
Agglutination is for the condenser of liquid and at least by the pump of the pressure reduction inside distillation still；Wherein, in the setting state of distillation still
Under, form the composition that agitating shaft extends in the horizontal direction.And in the decompression dehydration drying device, the waste of distillation still
Rabbling mechanism has the scraper plate slided on the inner surface of distillation still.The decompression dehydration drying device that the utility model provides can
Waste liquid, sewage, sludge, fecaluria the like waste are separated into solid constituent and liquid component, while can be by high-concentration waste gurry
It is separated into solid constituent and liquid component with difficult waste etc..
But the utility model heats the waste in distillation still using steam, the liquid component in waste
Condenser is imported after vaporization, and the steam that distillation still is discharged using the recirculated cooling water in condenser is needed to carry out heat exchange and is coagulated
Collect the liquid of obtained recycling.The heat of the steam of distillation still discharge is not used, and the waste entered in distillation still obtains
Less than preheating, the heating speed of waste is slow, and the thermal efficiency of system is low.
[invention content]
The technical problem to be solved in the present invention is to provide a kind of industrial wastes recovery and treatment methods that the thermal efficiency is high.
Another technical problems to be solved of the invention are to provide a kind of industrial wastes recovery and processing system that the thermal efficiency is high.
In order to solve the above-mentioned technical problem, the technical solution adopted by the present invention is a kind of industrial wastes recovery and treatment method,
The heat distributed within the condenser using condenser as waste liquid preheating device, using the waste liquid steam recycled from drain sump is to entering
Pending waste liquid before drain sump is preheated, cold to entering using the pending waste liquid before entrance drain sump as cooling medium
The waste liquid steam of condenser is condensed.
A kind of industrial wastes recovery and processing system, including drain sump, condenser and waste drains pump, drain sump include distillation still and
Rabbling mechanism, condenser include that steam discharge entrance, recovered liquid outlet, condensing medium inlet and condensing medium outlet, waste drains pump go out
Mouth connects the condensing medium inlet of condenser, and the condensing medium outlet of condenser connects the waste liquid entrance of distillation still；The steam discharge of distillation still
Outlet connects the steam discharge entrance of condenser.
Above-described industrial wastes recovery and processing system, including water vapor filtering device, recovered liquid measuring tank, recovered liquid
Storage tank and waste liquid metering device, water vapor filtering device be connected on condenser steam discharge entrance and distillation still exhaust vent it
Between；The outlet of waste liquid metering device connects the entrance of waste drains pump, and the entrance of recovered liquid measuring tank connects the recovered liquid outlet of condenser, returns
The outlet for receiving liquid measuring tank connects recovered liquid storage tank；Vacuum pump connects the vacuum access port of recovered liquid measuring tank by valve, recycling
The vacuum access port of liquid measuring tank is connected to the entrance of recovered liquid measuring tank.
Above-described industrial wastes recovery and processing system, distillation still include cylinder, heating jacket, front end-plate, end plate
It is exported with waste residue, heating jacket is tubular, is sleeved on the periphery of distillation kettle barrel；The exhaust vent be arranged in front end-plate or after
The top of end plate；Waste residue exports the lower end for being arranged in cylinder rear portion, passes through heating jacket；The medium inlet of heating jacket and medium
Outlet is in the lower part of heating jacket.
Above-described industrial wastes recovery and processing system, drain sump include residual cake valve and deslagging bend pipe, deslagging bend pipe peace
On the heating jacket of waste residue outlet lower section；Residual cake valve includes flap and cylinder, and waste residue outlet includes valve seat；Deslagging bend pipe
Crooked position includes mounting base, and mounting base includes rod aperture；The cylinder body of cylinder is fixed in mounting base, and the piston rod of cylinder is worn
Rod aperture is crossed, into deslagging bend pipe；Flap is mounted on the top of cylinder piston rod, is against on valve seat.
Above-described industrial wastes recovery and processing system, rabbling mechanism include the rotor being mounted in distillation still, rotor
Including main shaft and a plurality of agitating units axial arranged along main shaft, main shaft is supported by front end-plate and end plate by bearing；It stirs
It includes scraping plate mechanism to mix unit, and scraping plate mechanism includes scraper stent, elastic component and scraper plate assembly, and scraper plate assembly can be along main shaft radial direction
It is slidably mounted on scraper stent；Scraper plate assembly includes plural block and the inclined scraper plate of main-shaft axis；Scraper plate assembly includes scraping
The top surface of item, scraper plate is cambered surface, and scraping article is mounted on the top of scraper plate, plural block scraper plate is axially serially connected along main shaft, is scraped
The axis of item is parallel with the axis of main shaft, and the top surface of scraping article is bonded with cylinder inboard wall.
Above-described industrial wastes recovery and processing system, agitating unit include the scrapper conveyor described in two pieces of disc and two
Structure, two pieces of disc are fixed on main shaft along the axially spaced arrangement of main shaft in the middle part of disc；Two scraping plate mechanisms are mounted on two pieces
Between disc, the radial symmetric along main shaft is arranged；Scraper stent is fixed on the inside of disc, plate top surface is scraped outwardly, in cylinder
There are gaps for wall；Scraper plate assembly includes supporting plate and two guide rods, and the bottom of scraper plate is fixed on above supporting plate；The top of guide rod
It is fixed on supporting plate；Scraper stent is rectangular frame, including two pilot holes, guide rod are inserted into pilot hole, the two sliding
Cooperation；The elastic component includes two V-arrangement shrapnels, and V-arrangement shrapnel is mounted on the top plate of the supporting plate and scraper stent of scraper plate assembly
Between.
Above-described industrial wastes recovery and processing system, agitating unit include two mixing assemblies, and mixing assembly includes
Plural block and the inclined stirring wing of main-shaft axis, the rotation direction of stirring wing and scraper plate it is oppositely oriented；Two mixing assemblies are along main shaft
Radial symmetric arrangement, circumferential direction and scraping plate mechanism along main shaft are staggered 90 °.
Above-described industrial wastes recovery and processing system, disc are cross, the rotation direction of stirring wing be 35 ° of dextrorotation extremely
55 °, the rotation direction of scraper plate is that left-handed 40 ° to 60 ° adjacent agitating units are staggered 90 ° along the circumferential direction of main shaft, adjacent agitating unit
Share one piece of disc.
Above-described industrial wastes recovery and processing system, rotor include the hollow temperature monitoring stick of complex root, temperature prison
Survey axially spaced arrangement of the stick along main shaft；The inner end of temperature monitoring stick is fixed on main shaft, and main shaft is hollow shaft, including axial direction
Hole, the endoporus of temperature monitoring stick are connected to the axial hole of main shaft；One end of main shaft is equipped with conducting slip ring, is equipped in temperature monitoring stick
The signal wire of temperature sensor, temperature sensor passes through the axial hole of main shaft to be connect with conducting slip ring.
The industrial wastes recovery and processing system of the present invention within the condenser carries out pending waste liquid using waste liquid steam
Preheating, condenses waste liquid steam using pending waste liquid, and the heat of the steam of distillation still discharge is utilized, and is entered
Waste liquid before distillation still is preheated, and the heating speed of waste liquid is fast in distillation still, and the thermal efficiency of system is high.
[description of the drawings]
The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.
Fig. 1 is the front view of rabbling mechanism rotor of the embodiment of the present invention.
Fig. 2 is the vertical view of rabbling mechanism rotor of the embodiment of the present invention.
Fig. 3 is the sectional view of rabbling mechanism rotor of the embodiment of the present invention.
Fig. 4 is the stereogram of rabbling mechanism rotor of the embodiment of the present invention.
Fig. 5 is the left view of rabbling mechanism rotor of the embodiment of the present invention.
Fig. 6 is the front view of scraping plate mechanism of the embodiment of the present invention.
Fig. 7 is the vertical view of scraping plate mechanism of the embodiment of the present invention.
Fig. 8 is the side view of scraping plate mechanism of the embodiment of the present invention.
Fig. 9 is the axial sectional view of industrial wastes drain sump of the embodiment of the present invention.
Figure 10 is A in Fig. 9 to sectional view.
Figure 11 is the structure diagram of industrial wastes recovery and processing system of the embodiment of the present invention.
[specific implementation mode]
The structure of industrial wastes recovery and processing system of the embodiment of the present invention is as shown in figure 11, including drain sump, condenser, useless
Liquid pump, water vapor filtering device, recovered liquid measuring tank.Recovered liquid storage tank, waste liquid metering device and multiple pneumatic operated valves.
Drain sump includes distillation still and rabbling mechanism, and the outer of distillation still barrel is with heating jacket.
The outlet of waste liquid metering device connects the entrance of waste drains pump, and the outlet of waste drains pump connects the condensation of condenser by pneumatic operated valve
Medium inlet, the condensing medium outlet of condenser connect the waste liquid entrance of distillation still by pneumatic operated valve.
Water vapor filtering device is connected between the steam discharge entrance of condenser and the exhaust vent of distillation still, the steam discharge of distillation still
Outlet is connected to pneumatic operated valve for vacuum breaker.
The recovered liquid that the entrance of recovered liquid measuring tank connects condenser by pneumatic operated valve exports, and the outlet of recovered liquid measuring tank is logical
It crosses pneumatic operated valve and connects recovered liquid storage tank, vacuum pump connects the vacuum access port of recovered liquid measuring tank, recovered liquid metering by pneumatic operated valve
The vacuum access port of tank is connected to the entrance of recovered liquid measuring tank.In addition the vacuum access port of recovered liquid measuring tank is connected to gas
Dynamic valve is used for vacuum breaker.
The condenser of industrial wastes recovery and processing system of the embodiment of the present invention is used as waste liquid preheating device simultaneously, this hair
The industrial wastes of high concentration can be recycled by bright embodiment industrial wastes recovery and processing system.When system works, first will
Waste water utilization waste drains pump is evacuated in waste liquid preheating device (condenser), and the air inside drain sump is sucked out liquid-ring vacuum pump, waits for
Opened into waist valve when reaching certain vacuum inside drain sump, waste liquid sucked in drain sump, after the completion of feed liquor, to distillation still plus
The pneumatic angle pedestal valve that thermal jacket provides steam is opened, and steam is allowed to enter indirectly heat chuck, is conducted heat to barrel by heating jacket
Waste liquid is heated, at this time drain sump rabbling mechanism start, waste liquid is uniformly mixed, make its reach thermally equivalent effect
Fruit, when waste liquid reaches certain temperature under vacuum.Moisture content in waste liquid starts to evaporate, and the vapor that the moisture content in waste liquid is formed is logical
Water vapor filtering device is crossed, water vapor filtering device falls contaminant filter subsidiary in water vapour, and clean water steam is condensed
The coil pipe of (waste liquid preheating device) in device is condensed into water, condenser coil while preheating the waste liquid in waste liquid preheating device
The condensed water of outflow enters recovered liquid measuring tank, and condensed water drains into recovered liquid and deposits after recovered liquid measuring tank measures condensed water
Storage tank achievees the purpose that recycling, and the cost handled is very low,
Since when heating waste liquid, liquid-ring vacuum pump makes to keep certain vacuum degree inside distillation still, makes the boiling point of waste liquid
It reduces, under low temperature (50 DEG C) state, moisture content can evaporate the waste liquid in distillation still, be detached with impurity.Impurity in waste liquid
It forms solid to remain in distillation still, be discharged finally by slag-drip opening.
The efficiency that be dehydrated in distillation still can be substantially improved for preheating device, reduce half and use the steam that waste liquid heats
Amount.
The structure of industrial wastes drain sump of the embodiment of the present invention is as shown in Figures 9 and 10, including distillation still 100 and rabbling mechanism
Rotor 200.
Distillation still 100 includes metal cylinder 21, heating jacket 22, front end-plate 23, end plate 24, exhaust vent 2301 and useless
Slag outlet 2101, heating jacket 22 is tubular, is sleeved on the periphery of 100 metal cylinder 21 of distillation still.
The medium inlet 2201 of heating jacket 22 and media outlet 2202 are arranged in the lower part of heating jacket 22.It is input to and adds
Heat medium in thermal jacket 22 can also be deep fat with steam.
Exhaust vent 2301 is arranged in the top of front end-plate 23；Waste residue outlet 2101 is arranged under 21 rear portion of metal cylinder
End passes through heating jacket 22.
Deslagging bend pipe 25 is mounted on the heating jacket 22 of 2101 lower section of waste residue outlet；Residual cake valve includes flap 26 and cylinder
27, waste residue outlet 2101 forms a valve seat；The crooked position of deslagging bend pipe 25 has one there are one mounting base 2501 in mounting base
A rod aperture；The cylinder body of cylinder 27 is fixed in mounting base 2501, and the piston rod of cylinder passes through rod aperture, curved into deslagging
In the vertical pipeline of pipe 25；Flap 26 is mounted on the top of 27 piston rod of cylinder, is against on valve seat.
The structure of rabbling mechanism rotor 200 is as shown in Figures 1 to 8, including main shaft 1 and 6 stir along main shaft 1 is axial arranged
Unit is mixed, adjacent agitating unit mutually staggers 90 ° along the circumferential direction of main shaft 1
Agitating unit includes two pieces of disc, 2, two mixing assemblies and two scraping plate mechanisms.Disc 2 is cross, adjacent
Two scraping plate mechanisms share one piece of intermediate disc.
Along the axially spaced arrangement of main shaft 1, the middle part of disc 2 is fixed on main shaft 1 two pieces of disc 2.Two scraping plate mechanisms
Between two pieces of disc 2, the radial symmetric along main shaft 1 is arranged.
Scraping plate mechanism includes scraper stent 3, two panels V-arrangement shrapnel 4 and scraper plate assembly 5.Scraper stent 3 is rectangular frame, packet
Top plate 301, bottom plate 302 and two blocks of side plates 303 are included, the side plate 303 of scraper stent 3 is fixed on the inside of disc 2.
Scraper plate assembly 5 includes 502,5 pieces of the guide rod scraper plate 503 of supporting plate 501, two and a scraping article 504.
The bottom of scraper plate 503 is fixed on the top of supporting plate 501, and the top of guide rod 502 is fixed on 501 lower section of supporting plate.It scrapes
Plate 503 is tilted with 1 axis of main shaft, and the rotation direction of scraper plate is left-handed, and helical angle (inclination angle with 1 axis of main shaft) is 50 °.
Scraper plate 503 is soft scraper plate, and material is polytetrafluoroethylene (PTFE), and the top surface of scraper plate 503 is cambered surface, scrapes plate top surface outwardly, is pushed up
There are gaps for the inner wall of face and metal cylinder 21.Scraping article 504 is mounted on the top of scraper plate 503, by 5 pieces of scraper plates 503 along 1 axis of main shaft
To being serially connected, the axis of scraping article 504 is parallel with the axis of main shaft 1, and the top surface of scraping article 504 is bonded with the inner wall of cylinder 21.
Scraper plate assembly 5 is mounted on scraper stent 3 in which can be radially slided along main shaft 1.Scraper stent 3 there are two pilot hole,
The guide rod 502 of scraper plate assembly 5 is inserted into pilot hole, and the two is slidably matched.V-arrangement shrapnel 4 is mounted on scraper plate assembly 5 at two
Between supporting plate 501 and the top plate of scraper stent 3.
Mixing assembly includes two pieces and the inclined stirring wing 6 of 1 axis of main shaft, and the rotation direction of stirring wing 6 is 45 ° of dextrorotation.Two
Mixing assembly arranges that circumferential direction and the scraping plate mechanism along main shaft 1 are staggered 90 ° along the radial symmetric of main shaft 1.
Three hollow temperature monitoring sticks 7, axially spaced arrangement of the temperature monitoring stick 7 along main shaft 1 are mounted on main shaft 1.
The inner end of temperature monitoring stick 7 is fixed on main shaft 1, and main shaft 1 is hollow shaft, there are one axial hole 101, temperature monitoring stick 7 it is interior
Hole is connected to the axial hole 101 of main shaft 1.One end of main shaft 1 is equipped with conducting slip ring 102, and temperature sensing is housed in temperature monitoring stick 7
The signal wire 702 of device 701, temperature sensor passes through the axial hole 101 of main shaft 1 to be electrically connected with conducting slip ring 102.
The industrial wastes recovery and processing system of above example of the present invention utilizes waste liquid steam to pending within the condenser
Waste liquid preheated, waste liquid steam is condensed using pending waste liquid, the heat of steam of distillation still discharge obtains
It utilizes, the waste liquid entered before distillation still is preheated, and the heating speed of waste liquid is fast in distillation still, and the thermal efficiency of system is high.
The heating jacket of above example distillation still of the present invention is tubular, is sleeved on the periphery of distillation kettle barrel, can be to cylinder
Internal industrial wastes carries out 360 ° of heating, and heating speed is fast, and the thermal efficiency is high.
The scraper plate assembly of above example rotor of the present invention has a scraping article parallel with the axis of main shaft, the work of scraping article
Gap is not present between face and top tank structure, is capable of the waste residue of thorough cleaning dehydration top tank structure, it will not be because being dehydrated top tank structure waste residue knot
Coke causes the thermal efficiency to reduce.
Claims (10)
1. a kind of industrial wastes recovery and treatment method, which is characterized in that using condenser as waste liquid preheating device, using from dehydration
The heat that the waste liquid steam of tank recycling distributes within the condenser preheats the pending waste liquid before entering drain sump, will enter
As cooling medium, the waste liquid steam to entering condenser condenses pending waste liquid before drain sump.
2. a kind of industrial wastes recovery and processing system, including drain sump, condenser and waste drains pump, drain sump includes distillation still and stirs
Mechanism is mixed, condenser includes steam discharge entrance, recovered liquid outlet, condensing medium inlet and condensing medium outlet, which is characterized in that useless
The outlet of liquid pump connects the condensing medium inlet of condenser, and the condensing medium outlet of condenser connects the waste liquid entrance of distillation still；Distillation
The exhaust vent of kettle connects the steam discharge entrance of condenser.
3. industrial wastes recovery and processing system according to claim 2, which is characterized in that including water vapor filtering device,
Recovered liquid measuring tank, recovered liquid storage tank and waste liquid metering device, water vapor filtering device be connected on the steam discharge entrance of condenser with
Between the exhaust vent of distillation still；The outlet of waste liquid metering device connects the entrance of waste drains pump, and the entrance of recovered liquid measuring tank connects cold
The recovered liquid of condenser exports, and the outlet of recovered liquid measuring tank connects recovered liquid storage tank；Vacuum pump connects recovered liquid metering by valve
The vacuum access port of the vacuum access port of tank, recovered liquid measuring tank is connected to the entrance of recovered liquid measuring tank.
4. industrial wastes recovery and processing system according to claim 2, which is characterized in that distillation still includes cylinder, heating
Chuck, front end-plate, end plate and waste residue outlet, heating jacket is tubular, is sleeved on the periphery of distillation kettle barrel；The steam discharge goes out
Mouth is arranged in the top of front end-plate or end plate；Waste residue exports the lower end for being arranged in cylinder rear portion, passes through heating jacket；Heating folder
The medium inlet of set and media outlet are in the lower part of heating jacket.
5. industrial wastes recovery and processing system according to claim 2, which is characterized in that drain sump includes residual cake valve and row
Slag bend pipe, deslagging bend pipe are mounted on the heating jacket of waste residue outlet lower section；Residual cake valve includes flap and cylinder, waste residue outlet packet
Include valve seat；The crooked position of deslagging bend pipe includes mounting base, and mounting base includes rod aperture；The cylinder body of cylinder is fixed on mounting base
On, the piston rod of cylinder passes through rod aperture, into deslagging bend pipe；Flap is mounted on the top of cylinder piston rod, is against valve seat
On.
6. industrial wastes recovery and processing system according to claim 2, which is characterized in that rabbling mechanism includes being mounted on to steam
The rotor in kettle is evaporated, rotor includes main shaft and a plurality of agitating units axial arranged along main shaft, and main shaft is by front end-plate and rear end
Plate is supported by bearing；Agitating unit includes scraping plate mechanism, and scraping plate mechanism includes scraper stent, elastic component and scraper plate assembly, is scraped
Plate assembly can be radially slidably mounted on scraper stent along main shaft；Scraper plate assembly includes plural block and main-shaft axis is inclined scrapes
Plate；Scraper plate assembly includes scraping article, and the top surface of scraper plate is cambered surface, and scraping article is mounted on the top of scraper plate, by plural block scraper plate along main shaft
It is axially serially connected, the axis of scraping article is parallel with the axis of main shaft, and the top surface of scraping article is bonded with cylinder inboard wall.
7. industrial wastes recovery and processing system according to claim 6, which is characterized in that agitating unit includes two pieces of disc
With the scraping plate mechanism described in two, two pieces of disc are fixed on main shaft along the axially spaced arrangement of main shaft in the middle part of disc；Two
Scraping plate mechanism is mounted between two pieces of disc, and the radial symmetric along main shaft is arranged；Scraper stent is fixed on the inside of disc, scraper plate top
It faces outwardly, there are gaps with the inner wall of cylinder；Scraper plate assembly includes supporting plate and two guide rods, and the bottom of scraper plate is fixed on supporting plate
Top；The top of guide rod is fixed on supporting plate；Scraper stent is rectangular frame, including two pilot holes, guide rod are inserted into
In pilot hole, the two is slidably matched；The elastic component includes two V-arrangement shrapnels, and V-arrangement shrapnel is mounted on the supporting plate of scraper plate assembly
Between the top plate of scraper stent.
8. industrial wastes recovery and processing system according to claim 7, which is characterized in that agitating unit includes two stirrings
Assembly, mixing assembly include plural block and the inclined stirring wing of main-shaft axis, the rotation direction of stirring wing and scraper plate it is oppositely oriented；Two
A mixing assembly arranges that circumferential direction and the scraping plate mechanism along main shaft are staggered 90 ° along the radial symmetric of main shaft.
9. industrial wastes recovery and processing system according to claim 9, which is characterized in that disc is cross, stirring wing
Rotation direction be 35 ° to 55 ° of dextrorotation, the rotation direction of scraper plate is that left-handed 40 ° to 60 ° adjacent agitating units are staggered along the circumferential direction of main shaft
90 °, adjacent agitating unit shares one piece of disc.
10. industrial wastes recovery and processing system according to claim 6, which is characterized in that rotor includes that complex root is hollow
Temperature monitoring stick, axially spaced arrangement of the temperature monitoring stick along main shaft；The inner end of temperature monitoring stick is fixed on main shaft, main shaft
For hollow shaft, including axial hole, the endoporus of temperature monitoring stick is connected to the axial hole of main shaft；One end of main shaft is equipped with conductive sliding
Ring, temperature sensor is equipped in temperature monitoring stick, and the signal wire of temperature sensor passes through the axial hole of main shaft to connect with conducting slip ring
It connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810208809.1A CN108455693B (en) | 2018-03-14 | 2018-03-14 | Industrial waste liquid recycling system and recycling method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810208809.1A CN108455693B (en) | 2018-03-14 | 2018-03-14 | Industrial waste liquid recycling system and recycling method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108455693A true CN108455693A (en) | 2018-08-28 |
| CN108455693B CN108455693B (en) | 2023-11-17 |
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ID=63219870
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810208809.1A Active CN108455693B (en) | 2018-03-14 | 2018-03-14 | Industrial waste liquid recycling system and recycling method |
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| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002652A (en) * | 2019-04-29 | 2019-07-12 | 江苏惟亨环保科技有限公司 | Reclaiming system and process flow is concentrated in acid-bearing wastewater |
| CN110270120A (en) * | 2019-07-13 | 2019-09-24 | 深圳市科伟达超声波设备有限公司 | A kind of industrial wastes recovery and processing system |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5936583A (en) * | 1982-08-25 | 1984-02-28 | Hitachi Ltd | Treating device for heating steam and condensate of condenser for waste liquid |
| CN201823330U (en) * | 2010-10-09 | 2011-05-11 | 大和化学工业株式会社 | Pressure-reducing and dewatering drier |
| CN202580046U (en) * | 2012-05-29 | 2012-12-05 | 温州科瑞机械有限公司 | Pneumatic tank bottom valve |
| CN203593694U (en) * | 2013-05-10 | 2014-05-14 | 大和化学工业株式会社 | Waste disposal system |
| CN104086068A (en) * | 2014-07-10 | 2014-10-08 | 深圳市科伟达超声波设备有限公司 | Industrial liquid-containing sludge drying treatment device |
| CN106986486A (en) * | 2017-05-10 | 2017-07-28 | 南京工业大学 | A kind of highly salt containing organic waste water processing unit |
| CN206911206U (en) * | 2017-05-03 | 2018-01-23 | 河北晟凯新材料科技有限公司 | A kind of reactive flame retardant prepares and uses multi-angle stirring-type drying unit |
-
2018
- 2018-03-14 CN CN201810208809.1A patent/CN108455693B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5936583A (en) * | 1982-08-25 | 1984-02-28 | Hitachi Ltd | Treating device for heating steam and condensate of condenser for waste liquid |
| CN201823330U (en) * | 2010-10-09 | 2011-05-11 | 大和化学工业株式会社 | Pressure-reducing and dewatering drier |
| CN202580046U (en) * | 2012-05-29 | 2012-12-05 | 温州科瑞机械有限公司 | Pneumatic tank bottom valve |
| CN203593694U (en) * | 2013-05-10 | 2014-05-14 | 大和化学工业株式会社 | Waste disposal system |
| CN104086068A (en) * | 2014-07-10 | 2014-10-08 | 深圳市科伟达超声波设备有限公司 | Industrial liquid-containing sludge drying treatment device |
| CN206911206U (en) * | 2017-05-03 | 2018-01-23 | 河北晟凯新材料科技有限公司 | A kind of reactive flame retardant prepares and uses multi-angle stirring-type drying unit |
| CN106986486A (en) * | 2017-05-10 | 2017-07-28 | 南京工业大学 | A kind of highly salt containing organic waste water processing unit |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002652A (en) * | 2019-04-29 | 2019-07-12 | 江苏惟亨环保科技有限公司 | Reclaiming system and process flow is concentrated in acid-bearing wastewater |
| CN110270120A (en) * | 2019-07-13 | 2019-09-24 | 深圳市科伟达超声波设备有限公司 | A kind of industrial wastes recovery and processing system |
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| CN108455693B (en) | 2023-11-17 |
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