CN104926642B - A kind of process units of essence dimeric dibasic acid - Google Patents
A kind of process units of essence dimeric dibasic acid Download PDFInfo
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- CN104926642B CN104926642B CN201510362369.1A CN201510362369A CN104926642B CN 104926642 B CN104926642 B CN 104926642B CN 201510362369 A CN201510362369 A CN 201510362369A CN 104926642 B CN104926642 B CN 104926642B
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
Abstract
The present invention discloses the process units of a kind of essence dimeric dibasic acid, and described process units is included centrifugal separating device, membrane evaporator and molecular distillation apparatus the most successively by technological process.Described process units also includes high-temperature waste gas treating apparatus and wastewater treatment equipment, the steam evaporated through described membrane evaporator and the isolated organic exhaust gas of described molecular distillation apparatus are carried out condensation separation process by described high-temperature waste gas treating apparatus, described wastewater treatment equipment by essence dimeric dibasic acid production process in and high-temperature waste gas treating apparatus produce waste water carry out purified treatment.The present invention has that technique is simple, dephosphorization efficiency is high, reduces equipment manufacturing cost, purification efficiency is high, have twice condensation function, produce the advantage that purification of waste water is effective.
Description
Technical field
The present invention relates to the preparation field of dimeric dibasic acid, particularly relate to the process units of a kind of essence dimeric dibasic acid.
Background technology
Dimeric dibasic acid, is often referred to dimer (fatty acid) yl, is the mixture of a kind of complicated component, because main component contains
Two hydroxy-acid groups and gain the name.It is to use unsaturated fatty acid, if oleic acid and linoleic acid are by mutual polymerization etc.
Obtain.Dimeric dibasic acid has excellent heat stability, and can keep mobility within the scope of the widest temperature.
Dimeric dibasic acid is currently mainly used as synthesizing polyamides, and there are about half in the neutral polyamide synthesized and be used to preparation
PUR, secondly for the production of ink.
The domestic method preparing dimeric dibasic acid is clay catalytic method, and the method is existing two kinds of techniques: one is fat
Fatty acid methyl esters method, with various fatty acid methyl esters as raw material, montmorillenite is catalyst, with methanol deoxygenation.
This technique advantage be equipment be simple and convenient to operate, product quality preferable.But catalyst amount is relatively big,
The purity requirement of methanol is higher.Another kind is fatty acid direct polymerization technique, and employing vegetable oil acid is raw material,
In the case of nitrogen charging, after having reacted, decolour, filter, prepare rough dimeric dibasic acid, then steamed by thin film
Send out in device and distill, obtain smart dimeric dibasic acid finished product.This process recovery ratio is high, steady quality, for domestic current production two
The main technique of polyacids.
At present, essence dimeric dibasic acid is some deficiency below existence when producing: one, and centrifugal separating device is the most only
There is heavy out and light phase export, after doing Oil-water separation, aqueous phase is the thinnest with the interface of oil phase, heavy out
Certain oil can be taken out of, and light phase export also can take certain water out of, separate insufficient, cause dephosphorization efficiency
Low；And the production method of a kind of dimeric dibasic acid described in the patent application of Patent publication No CN103012110 uses
Two step method dephosphorization, first washes, then carries out secondary dephosphorization by centrifugal separating device.This method requirement
Plurality of devices with the use of, there is complex process, ineffective weak point.Its two, through thin film steam
Device evaporates high temperature organic exhaust gas process and does not cuts at the end, can cause environment pollution.Three, one, existing
Smart dimeric dibasic acid production process in the waste water that produces after Sedimentation tank and regulating reservoir process, typically directly enter
AO pond carries out organic decomposition.Do not carry out Oil-water separation owing to being directly entered the waste water in AO pond, increase the weight of
The decomposition burden in AO pond；Its two, containing substantial amounts of suspension granule in waste water, be suspended in waste water,
Not easy-clear.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, it is provided that a kind of technique is simple, dephosphorization efficiency is high, reduce equipment
Cost, purification efficiency are high, have twice condensation function, produce a kind of essence dimeric dibasic acid that purification of waste water is effective
Process units.
The present invention uses techniques below means to solve above-mentioned technical problem: the process units of a kind of essence dimeric dibasic acid,
Described process units is included centrifugal separating device, membrane evaporator the most successively and divides by technological process
Sub-distilling apparatus；Described process units also includes high-temperature waste gas treating apparatus and wastewater treatment equipment, described
The steam evaporated through described membrane evaporator and described molecular distillation apparatus are divided by high-temperature waste gas treating apparatus
The organic exhaust gas separated out carries out condensation separation process, and described wastewater treatment equipment is by essence dimeric dibasic acid production process
And the waste water that high-temperature waste gas treating apparatus produces carries out purified treatment；Described wastewater treatment equipment includes sedimentation
Pond, oil interceptor, anaerobic pond, neutralization pond, flotation tank, first stage precipitation tank, aerobic pond and second-level settling pond；
Described centrifugal separating device includes centrifuge, separating tank and drain pipe；Described centrifuge include housing, on
Lid, rotary drum, light phase weir, heavy phase weir；Described rotary drum is arranged on the center of described housing, described light phase weir
Being arranged on the open area at described rotary drum top, described heavy phase weir is arranged on the bottom of described upper cover；Described shell
The 3rd charging aperture, the first water inlet, light phase export and heavy out is offered on body；Described 3rd charging
Mouth and described first water inlet are positioned at described light phase export and the lower section of described heavy out；Cover out on described
Being provided with the first row mouth of a river, the described first row mouth of a river is docked mutually with described drain pipe, and described drain pipe is provided with
Second elevator pump；Described separating tank is arranged on the lower section of described heavy out, is provided with gear in described separating tank
Plate, there is gap with the bottom of described separating tank inwall in the bottom of described baffle plate；
Described high-temperature waste gas treating apparatus includes ventilate tank, the second pipe bundle condenser, coil pipe and refrigerating plant；
The lower end of described ventilation tank offers air inlet；Described coil pipe is arranged on the inside of described ventilation tank in the shape of a spiral
In cavity, the bottom of described coil pipe is provided with water inlet, and the top of described coil pipe is provided with outlet, described
The water inlet of coil pipe and the outlet of described coil pipe all extend to outside the tank body of described ventilation tank；Described coil pipe
The discharge outlet of water inlet and described refrigerating plant interlink, the outlet of described coil pipe and described refrigerating plant
Water inlet interlink；Described second pipe bundle condenser is arranged on the top of described ventilation tank, described secondary series
The bottom of pipework condensation device is interlinked by the top of the second airway with described ventilation tank, and described second tubulation is cold
The top of condenser connects downtake pipe；
Described Sedimentation tank, oil interceptor, anaerobic pond, neutralization pond, flotation tank, first stage precipitation tank, aerobic pond with
And second-level settling pond is set gradually from front to back by technological process；Waste water is carried out solid-liquid separation by described Sedimentation tank,
Waste water is carried out aqueous phase-separation of oil by described oil interceptor；Described oil interceptor is configured with suction pump, described suction pump
By in isolated waste water lifting to anaerobic pond；Organic substance in waste water is decomposed by described anaerobic pond, institute
Stating neutralization pond and the waste water after anaerobic pond processes is neutralized process, the bottom of described flotation tank is provided with blows
Wind apparatus, the particle in described flotation tank waste water is blown to liquid by described blowing device by described flotation tank
Face, and the waste water below superposed layer is carried and precipitates into described first stage precipitation tank；Described aerobic pond is to inflow
Waste water therein carries out nitration treatment；Waste water therein for inflow is settled by described second-level settling pond again.
Preferably: offer on the inwall of described rotary drum and be equipped with temperature control equipment, described temperature control equipment bag
Including temperature detector, electronic heater and add heat pipe, the temperature test scope of described temperature detector is (50-100) DEG C.
Preferably: its temperature range of water flowed into through described water inlet is (85-95) DEG C.
Preferably: described baffle plate is welded on the sidewall of described separating tank internal cavities, is divided by described separating tank
It is the first cavity and the second cavity；Described gap is (1-5) cm.
Preferably: described centrifugal separating device also includes heavy phase discharge pipe, and described heavy phase discharge pipe is provided with
3rd elevator pump, described heavy phase discharge pipe one end be connected with described heavy out, described heavy phase discharge
The other end of pipe extends in described first cavity or extends in described second cavity, described heavy phase discharge pipe
It is connected with described heavy out；Described separating tank is provided with band and stays the universal wheel of dynamic device.
Preferably: the bottom of described ventilation tank is further opened with waste liquid outlet, described high-temperature waste gas treating apparatus
Also include waste collecting device；Described waste collecting device includes catheter and waste collection tank, described useless
The top of liquid collecting tank is connected with described ventilation tank by described catheter.
Preferably: on described waste collection tank, be further opened with automatic draining device, described automatic draining device bag
Including the second liquid level sensor and electronics lock, described second liquid level sensor is arranged on described waste collection tank
On inwall, described electronics lock is arranged at the leakage fluid dram of described waste collection tank.
Preferably: described second pipe bundle condenser is provided with the second deflection plate, described second deflection plate and institute
State the condensing tube in the second pipe bundle condenser to be connected.
Preferably: the water side of described coil pipe is additionally provided with the 6th and carries material pump.
Preferably: in described neutralization pond, be provided with pH regulator instrument, described wastewater treatment equipment also includes mud pressure
Filter device and sterilization pool, described sludge press filtration device is in order to the mud being precipitated out by described second-level settling pond
Carry out being dehydrated concentration；The water inlet of described sterilization pool is connected with the outlet of described second-level settling pond,
Described second-level settling pond is the one of vertical sedimentation basin, radical sedimentation basin or rectangular sedimentation tank；Described
Sedimentation tank, described oil interceptor, described anaerobic pond, described neutralization pond, described flotation tank, described one-level precipitate
Pond, described aerobic pond, described second-level settling pond and described sterilization pool are expoxy glass steel structure water pond,
Described sludge press filtration device is configured with Pulp pump.
It is an advantage of the current invention that: by traditional washing dephosphorization and centrifugation dephosphorization are combined,
Improve the efficiency of dephosphorization, simplify equipment.Simultaneously as its temperature of water added is (85-95) DEG C,
It is prone to vaporization discharge.And it is provided with temperature control equipment, there is the temperature within auto-adjustment control rotary drum
Effect.
High-temp waste gas is passed through in tank from the air inlet of ventilation tank, by the condensation of coil pipe, high temperature is given up
In gas, a part of waste gas condensation is to liquid, falls in collecting tank.The waste gas of uncooled one-tenth liquid passes through secondary series
The effect of pipework condensation device, carries out time condensation, further waste gas is carried out condensation cleaning process, through secondary series
The condensed waste liquid of pipework condensation device falls into equally to collecting tank, it is achieved the purpose of twice time condensation function.
Further, the second pipe bundle condenser is provided with the second deflection plate, plays the effect of fixing support.Due to
The bottom of ventilation tank is provided with waste collecting device, can take out sample at any time in waste collection tank, thus examine
The harmful components of test specimens.When the liquid level of waste collection tank is higher than setting value, the second liquid level sensor send out
Go out induced signal, drive electronics lock to open, the waste liquid of excess is discharged, it is achieved the function of automatic drain.
Oil interceptor is set between Sedimentation tank and anaerobic pond, by the effect of oil interceptor so that proportion is lighter
The floating aqueous phase heavier with proportion of oil phase is supreme, and by suction pump by isolated waste water lifting to anaerobic pond
Reach the effect of Oil-water separation.Flotation tank is set between neutralization pond and first stage precipitation tank, by flotation tank
Bottom is provided with blowing device, and the particle in described flotation tank waste water is blown to liquid level, and by superposed layer
Following waste water carries in first stage precipitation tank, alleviates cleaning load.
Accompanying drawing explanation
Fig. 1 is the structured flowchart of the embodiment of the present invention.
Fig. 2 is the structural representation of polyplant in the embodiment of the present invention.
Fig. 3 is the structural representation of transfer still in the embodiment of the present invention.
Fig. 4 is the structural representation of centrifugal separating device in the embodiment of the present invention.
Fig. 5 is the structural representation of pipeline switch filtering device in the embodiment of the present invention.
Fig. 6 is the structural representation of flange in the embodiment of the present invention.
Fig. 7 is the structural representation of polycondensation device in the embodiment of the present invention.
Fig. 8 is the structural representation of defecator in the embodiment of the present invention.
Fig. 9 is the structural representation of distributing device in the embodiment of the present invention.
Figure 10 is the structural representation of pelletize conveying mechanism in the embodiment of the present invention.
Figure 11 is the structural representation of automatic spraying device in the embodiment of the present invention.
Figure 12 is the partial perspective view of pelletize grading discharge mechanism in the embodiment of the present invention.
Figure 13 is the structural representation of pelletize grading discharge mechanism in the embodiment of the present invention.
Figure 14 is the structural representation of emission-control equipment in the embodiment of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in detail.
As it is shown in figure 1, the present embodiment include the most successively by technological process polyplant, acidifying still,
Filter press, transfer still, centrifugal separating device, membrane evaporator, molecular distillation apparatus, pipeline switch
Defecator, polycondensation device, defecator and prilling granulator.Described process units also includes exhaust-gas treatment
Device and wastewater treatment equipment, the waste gas produced in production process carries out decomposing by described emission-control equipment,
Settlement treatment, described wastewater treatment equipment by production process and emission-control equipment produce waste water carry out
Purified treatment.
Described acidifying still, described filter press, described membrane evaporator and described molecular distillation apparatus are equal
For existing equipment.
As in figure 2 it is shown, polyplant includes polymeric kettle 101 and carries material device 102, described polymeric kettle 101
Including polymerization kettle 1011 and polymerization kettle cover 1012, described polymerization kettle cover 1012 offers the first charging
Mouth 1013.The described material device 102 that carries includes storage tank the 1021, first elevator pump 1022 and the first guide
Pipe 1023.One end of described first passage 1023 is connected with described first charging aperture 1013, and described first
The other end of passage 1023 is connected with the discharging opening of described storage tank 1021, described first elevator pump 1022
It is arranged on described first passage 1023.
As it is shown on figure 3, described transfer still includes transfer still shell body 401 and contact autoalarm 402,
Offering the second charging aperture 403 on described transfer still shell body 401, described contact autoalarm 402 wraps
Include the first liquid level sensor 4021 and alarm device 4022.Described first liquid level sensor 402 is suspended on institute
Stating in the internal cavities of transfer still shell body 401, described first liquid level sensor 4021 sends induced signal and drives
Described alarm device 4022 sends alarm signal.
As shown in Figure 4, described centrifugal separating device includes centrifuge, separating tank and drain pipe 503.Described
Centrifuge includes housing 5011, upper cover 5012, rotary drum 5013, light phase weir 5014, heavy phase weir 5015.Institute
Stating rotary drum 5013 and be arranged on the center of described housing 5011, described light phase weir 5014 is arranged on described rotary drum
The open area at 5013 tops, described heavy phase weir 5015 is arranged on the bottom of described upper cover 5012.Described shell
The 3rd charging aperture the 5016, first water inlet 5017, light phase export 5018 and heavy phase is offered on body 5011
Outlet 5019.Described 3rd charging aperture 5016 and described first water inlet 5017 are positioned at described light phase export 5018
Lower section with described heavy out 5019.The first row mouth of a river 50110 is offered on described upper cover 5012, described
The first row mouth of a river 50110 is docked with described drain pipe 503 phase, described drain pipe 503 is provided with second and carries
Rise pump 504.Described separating tank 502 is arranged on the lower section of described heavy out 5019, described separating tank 502
In be provided with baffle plate 5023, between the bottom of the bottom of described baffle plate 5023 and described separating tank 502 inwall exists
Gap.
Offer on the inwall of described rotary drum 5013 and be equipped with temperature control equipment 5021, described temperature control equipment bag
Include temperature detector 50211, electronic heater 50212 and add heat pipe 50213, the temperature of described temperature detector 50211
Degree test scope is (50-100) DEG C.Its temperature range of water flowed into through described first water inlet 5017 is
(85-95) DEG C, described baffle plate 5023 is welded on the sidewall of described separating tank 502 internal cavities, by described
Separating tank is divided into the first cavity 5021 and the second cavity 5022.Described gap is (1-5) cm, described from
Heart segregation apparatus 5 also includes heavy phase discharge pipe 505, and described heavy phase discharge pipe 505 is provided with the 3rd elevator pump
506, described heavy phase discharge pipe 505 one end be connected with described heavy out 5019, described heavy phase arrange
The other end going out pipe 5023 extends to (to extend to described second cavity 5022 in described first cavity 5021
In).Described heavy phase discharge pipe 505 is connected with described heavy out 5019, and described separating tank is provided with band and stays
The universal wheel 5024 of dynamic device.
As seen in figs. 5-6, described pipeline switch filtering device include the first feed pipe 701, surge tank 702,
Siphunculus more than first 703, several filtering tanks 704, connecting tube 705 and return duct 706.Described return duct
The 4th elevator pump 707 it is provided with on 706.Described siphunculus more than first 703 is tee T, and described tee T is by erecting
Pipe 7031 and transverse tube 7032 form.Described filtering tank 704 includes that the first filtering tank 7041 and second filters
Tank 7042.Described vertical tube 7031 is connected with the discharging opening of described surge tank 702, described transverse tube 7032
One end is connected with described first filtering tank 7041 by the first flange 708, another of described transverse tube 7031
End is connected with described second filtering tank 7042 by the second flange 709.The feeding mouth of described connecting tube 705
Being connected by the discharging opening of three-flange 7010 with described first filtering tank 7041 (can also be with the second filtering tank
The discharging opening of 7042 is connected), the discharging opening of described connecting tube 705 by the 4th flange 7011 with described time
Flow tube 706 is connected.Described vertical tube 7031 is additionally provided with main valve 7033, at described transverse tube 7031
Two ends are provided with point valve 7034, and all flanges all include fixed flange 7015, mounting flange 7016
And securing member 7017.Described fixed flange 7015 is by described securing member 7017 and described adpting flange
Dish 7016 connects into entirety, is additionally provided with close between described fixed flange 7015 and mounting flange 7016
Packing 7018, the surface-coated of described sealing gasket 7018 has waterproof, anticorrosive coat (being not drawn in figure).
As it is shown in fig. 7, described polycondensation device includes polycondensation vessel 801, Dropping feeder 802, first row pipework condensation
Device 803 and the first airway 804.Described first pipe bundle condenser 803 is by described first airway 804
Being connected with the internal cavities of described polycondensation vessel 801, described Dropping feeder 802 includes fluid reservoir 8021, leads
Liquid pipe 8022 and valve 8023.One end of described catheter 8022 and the discharging opening of described fluid reservoir 8021
Being connected, the other end of described catheter 8022 extends in the internal cavities of described polycondensation vessel 801, described
Valve 8023 is arranged on described catheter 8022.Described first pipe bundle condenser 803 is provided with first
Deflection plate 805, described first deflection plate 805 is connected with the condensing tube in described first pipe bundle condenser 803；
Described polycondensation vessel 801 includes that polycondensation kettle 8011 and polycondensation kettle cover 8012, described polycondensation kettle 8011 wrap
Include interior tank body 80111 and outer tank body 80112, described outer tank body 80112 offers the first oil-in and the
One oil-out.Fluid is stored, institute at cavity between described interior tank body 80111 and described outer tank body 80112
State and on kettle cover 8012, offer the 4th charging aperture.Described polycondensation device 8 also includes automatic temp controller 805,
Described automatic temp controller 805 includes temperature sensor 8051, circulating pipe, circulating pump 8053, electronic valve
8054 and fuel reserve tank 8055.Described temperature sensor 8051 is arranged in described outer tank body 80112, institute
State circulating pump 8053 and described electronic valve 8054 is arranged on described circulating pipe.Described fuel reserve tank 8055
On offer the second oil-in and the second oil-out, described circulating pipe 8055 include oil inlet pipe 80551 with
And flowline 80552.Described first oil-in is connected by described oil inlet pipe 80551 with described second oil-out
Logical, described first oil-out is connected by described flowline 80552 with described second oil-in.
Described polycondensation device also includes thermal insulation protection set 806, and described polycondensation vessel 801 is set in described thermal insulation protection
In set 806.Described circulating pump 8053 is arranged on described oil inlet pipe 80551, and described electronic valve 8054 sets
Put on described flowline 80552.It is additionally provided with power governor 8058 on described circulating pump 8053.Described
The outside of thermal insulation protection set 806 is provided with non-contact inductive alarm device 807, described non-contact inductive report
Alarm device 807 includes infrared sensor, processor and acoustic-optic alarm.Described infrared sensor defeated
Go out end to be connected with the input of described processor, the outfan of described processor and described acoustic-optic alarm
Input is connected.
As shown in Figure 8, described defecator includes filter the 901, second feed pipe the 902, first discharge nozzle
903 and oil pipe 904.Described second feed pipe 902 includes the second charging inner tube 9021 and the second charging
Outer tube 9022, described first discharge nozzle 903 includes the first discharging inner tube 9031 and the first discharging outer tube 9032,
At cavity between inner tube outer tube corresponding thereto, storage has fluid.Described second charging outer tube 9022 is with described
One end of oil pipe 904 is connected, and described first discharging outer tube 9032 is connected with the other end of described oil pipe 904
Logical.Described first discharging inner tube 9031 and described second charging inner tube 9021 all with described filter 901
Internal cavities communicate.
Described defecator also includes the 5th flange 905 and the 6th flange 906, described second charging outer tube
9022 are connected by described 5th flange 905 with one end of described oil pipe 904, described first discharging outer tube
9032 are connected by the 6th flange 907 with the other end of described oil pipe 904.Also set on described oil pipe 904
Being equipped with automatic heating device 907, described heater 907 includes temperature controller and heater, described in add
Portable power source interface 908 it is additionally provided with on hot device.Described temperature controller includes display screen and controls device,
It is provided with USB interface 909 on described control device.Described filter 901 include protective housing 9011 and
It is arranged on the filter assemblies 9012 within described protective housing.
As it is shown in figure 1, described prilling granulator includes granulating mechanism the most successively, makes according to technological process
Grain conveying mechanism and pelletize grading discharge mechanism.
As shown in figs. 9-10, described granulating mechanism includes that distributing device and actuating device, described distributing device include
Granulating cylinder 100111 and pellet device 100112.Described pellet device 100112 includes grain-cutter 1001121
And power transmission shaft 1001122, described grain-cutter 1001121 is set in described power transmission shaft 1001122, described
The main part of power transmission shaft 1001122 is housed in the cavity of described granulating cylinder 100111, described power transmission shaft
The two ends of 1001122 are all extended outside the cavity of described granulating cylinder 100111.The end of described granulating cylinder 100111
Portion offers the material hole 100113 that several are regularly arranged, and the top of described granulating cylinder 100111 offers feeding
Mouth 100114, described material hole 100113, described spout 100114 and described cavity intercommunication.Described transmission
Device includes motor the 100122, first gear the 100121, second gear 100123 and chain 100124,
Described chain 100124 is set on described first gear 100121 and the second gear 100123, described electricity
The output shaft of machine 100122 is connected with described first gear 100121, and described second gear 100123 is with described
The end of power transmission shaft 1001122 is connected.
Described actuating device also includes that Tension gear 100125, described Tension gear 100125 are positioned at described first
Between gear 100122 and described second gear 100123 and be arranged on the inner side of described chain 100124.Institute
Stating a diameter of 0.8mm in material hole 100113, the outside of described spout 100114 is provided with sealing lid
100115, the described lid 100115 that seals uses with described spout 100114 and to threaded.Described granulating mechanism
Also include that two secondary bracing frames 10013, described two secondary bracing frames 10013 are oppositely arranged, described granulating cylinder 100111
Two ends be arranged on corresponding bracing frame 10013, described grain-cutter 1001121 overlaps in the shape of a spiral
It is located in described power transmission shaft 1001122.
As shown in figs. 10-11, described pelletize conveying mechanism includes conveyer device, and described conveyer device will be through pelletize
The particle that cylinder 100111 flows out transmits.Described conveyer device includes drivewheel 100211, driven pulley 100212
And drapery panel 100213, described drapery panel 100213 is set in described drivewheel 100211 and driven pulley
On 100212.Described conveyer device also includes that some pieces pat plate 100214, described in pat plate 100214 and hang down
Directly the conveying direction in described drapery panel is fixed on lower layer mix feeding plate 100213, and pats plate described in guarantee
The length direction of 100214 is paralleled with the width of described drapery panel 100213.At described conveyer device
Side is additionally provided with several automatic spraying devices 10022.The waste gas that is arranged above of described conveyer device is received
Acquisition means, described waste gas collection device includes extractor fan 100231 and ventilation shaft 100232.Described take out
Wind apparatus 100231 is arranged on the top of described granulating cylinder 100111, one end of described ventilation shaft 100232
Being connected with described extractor fan 100231, the other end of described ventilation shaft 100231 is parallel to described conveying
The length direction of device extends to the top of described delivery device tip.The bottom of described ventilation shaft 100232
It is provided with some row's ventilation holes 100233.
The described length patting plate 100214 is not shorter than the width of described drapery panel 100213, described in pat plate
The bottom of 100214 is coated with smooth layer (being not drawn in figure).Described pat the two of plate 100214 length direction
End is respectively welded fixing bar (being not drawn in figure), and the bottom of described fixing bar fixes on the ground.Described from
Dynamic spray equipment 10022 includes shower nozzle 100221, heat induction apparatus, receiver, electric controller, water pump
100222 and water tank 100223.Described shower nozzle 100221 is fixed on the top of described drapery panel 100213,
Described heat induction apparatus is distributed in, in order to test, the heat that on drapery panel 100213, particle is distributed.The described collection of letters
Machine is in order to accept the signal that described heat induction apparatus sends, and described pneumoelectric controller accepts described receiver and sends
Information and drive described water pump 100222 to draw water by motor.
As illustrated by figs. 12-13, described pelletize grading discharge mechanism include scraper 10031, sieve 10032, under
Funnel 10033, hair-dryer 10034, segregation apparatus the 10035, second discharge nozzle 10036, floccule are received
Acquisition means 10037 and siphunculus 10038 more than second.The edge of a knife of described scraper 10031 abuts in described conveying dress
On the drapery panel 100213 of set terminal, described in sieve and 10032 be arranged on the lower section of described scraper 10031 solid
It is scheduled on the opening of described lower funnel 10033, the bottom of described lower funnel 10033 and described more than second
Siphunculus 10038 is to connection.The arrival end of described siphunculus more than second 10038 be provided with described hair-dryer 10034,
The outlet of described porous pipe line is connected with the entrance of described segregation apparatus 10035, described segregation apparatus 10035
On offer floccule outlet, the bottom of described segregation apparatus 10035 offers discharging opening.Described floccule
Outlet 10035 is connected with described floccule collection device 10037 by described second passage 10036.
Described second discharge nozzle 10036 is connected with the discharging opening of described segregation apparatus 10035.Described segregation apparatus
The discharge outlet of 10035 is provided with side tool lock 100310, and described second passage 10036 is provided with the 5th
Elevator pump 100311.
Described sieve 10032 mesh diameter be (0.6-1.1) mm, the opening of described lower funnel 10033
Port footpath with described sieve 10032 equal in magnitude.Described side tool lock 100310 includes striker plate 1003101
And the discharging opening of handle of a knife 1003102, one end of described striker plate 1003101 and described segregation apparatus 10035
Hinged, the other end of described striker plate 1003101 is provided with described handle of a knife 1003102.Described blower fan 10034
On be additionally provided with PCU Power Conditioning Unit 100341, described PCU Power Conditioning Unit 100341 is transformator.Described make
Grain grading discharge mechanism also includes that two pieces of fixed plates 10039, described two pieces of fixed plates 10039 are oppositely arranged on institute
State the both sides of the end of conveyer device.Be provided with groove 100391 on every piece of fixed block 10039, described in scrape
The two ends of cutter 10031 are respectively welded screw rod 100311, described screw rod 100311 and described groove 100391
Employing is slidably connected, and every screw rod 100311 is also arranged with two nuts 100312, and nut is close to respectively
The both sides of corresponding groove.
As it is shown in figure 1, described emission-control equipment includes high-temperature waste gas treating apparatus, spray the most successively
Drench and purify exhaust device and odor removal.
As shown in figure 14, described high-temperature waste gas treating apparatus includes tank the 12011, second pipe bundle condenser of ventilating
12012, coil pipe 12013 and refrigerating plant 12014.The lower end of described ventilation tank 12011 offers air inlet
Mouthful, described coil pipe 12013 is arranged in the internal cavities of described ventilation tank 12011 in the shape of a spiral, described dish
The bottom of pipe 12013 is provided with water inlet, and the top of described coil pipe 12013 is provided with outlet, described dish
The water inlet of pipe 12013 and the outlet of described coil pipe 12013 all extend to described ventilation tank 12011
Outside tank body.The water inlet of described coil pipe 12013 interlinks with the discharge outlet of described refrigerating plant 12014, institute
The water inlet of the outlet and described refrigerating plant 12014 of stating coil pipe 12013 interlinks.Described second tubulation
Condenser 12012 is arranged on the top of described ventilation tank 12011, described second pipe bundle condenser 12012
Bottom is interlinked by the top of the second airway 12015 with described ventilation tank 12011, described second tubulation
The top of condenser 12012 connects downtake pipe 12016.
Described spray cleaning exhaust device include the first air inlet pipe 12021, at least one spray agent set and
Second exhaust pipe 12023.The lower end of described spray agent set 12022 offers the first air intake, described spray
The top drenching agent set 12022 offers first row QI KOU, being internally provided with of described spray agent set
Spray equipment 12024, the lower end of described spray agent set offers waste liquid outlet 10228.Described first
The outlet of air inlet pipe 12021 is connected with described first air intake, described first row QI KOU and described second row
Trachea 12023 is connected.
Described odor removal includes the 3rd air inlet pipe 12031, deodorization agent set 12032 and the 3rd exhaustor
12033.The internal cavities of deodorization agent set 12032 is hung with some pieces of biomembranes 12034.Described 3rd
The outlet of air inlet pipe 12031 is connected with the air inlet of described deodorization agent set 12032, described deodorization master
The air vent of body device 12032 is connected with described 3rd exhaustor 12031.
The bottom of described ventilation tank 12011 is further opened with waste liquid outlet, and described high-temperature waste gas treating apparatus is also
Including waste collecting device.Described waste collecting device includes catheter 120181 and waste collection tank
120182, the top of described waste collection tank 120182 is by described catheter 120181 and described ventilation tank
The waste liquid outlet of 12011 is connected.It is further opened with automatic draining device on described waste collection tank 120182,
Described automatic draining device includes the second liquid level sensor 120191 and electronics lock 120192, described second liquid
Level sensor 120191 is arranged on the inwall of described waste collection tank 120182, described electronics lock 120192
It is arranged at the leakage fluid dram of described waste collection tank 12018.Described second pipe bundle condenser 12012 is arranged
There is the second deflection plate 120121, in described second deflection plate 120121 and described second pipe bundle condenser 12012
Condensing tube be connected.The water side of described coil pipe 12013 is additionally provided with the 6th and carries material pump 10120131.
Described spray agent set 12022 includes that the first spray agent set 120221, second sprays main body dress
Put 120222 and connect described first spray agent set 120221 and the second spray agent set
Second air inlet pipe 120223 of 120222, is provided with the 7th elevator pump in described second air inlet pipe 120222
12025。
Described biomembrane 12034 includes adsorption layer 120341, anaerobic layer 120342, aerobic the most respectively
Layer 120343 and filter material layer 120344.
As it is shown in figure 1, described wastewater treatment equipment include the most successively by technological process Sedimentation tank, every
Oil sump, anaerobic pond, neutralization pond, flotation tank, first stage precipitation tank, aerobic pond and second-level settling pond.Described
Waste water is carried out solid-liquid separation by Sedimentation tank, and waste water is carried out aqueous phase-separation of oil by described oil interceptor.Described oil removal
Pond is configured with suction pump, and described suction pump is by isolated waste water lifting to anaerobic pond.Described anaerobic pond pair
Organic substance in waste water decomposes, and described neutralization pond is neutralized process to the waste water after anaerobic pond processes,
The bottom of described flotation tank is provided with blowing device, described flotation tank by described blowing device by described air supporting
Particle in the waste water of pond blows to liquid level, and carries entering into described first stage precipitation tank by the waste water below superposed layer
Row precipitation.Described aerobic pond carries out nitration treatment to flowing into waste water therein；Described second-level settling pond will flow into
Waste water therein settles again.
Described neutralization pond is provided with pH regulator instrument, described anaerobic pond and described Aerobic Pond all piled up active
Mud.Described wastewater treatment equipment also includes sludge condensation filter-pressing device and sterilization pool, described sludge press filtration
Device carries out being dehydrated concentration in order to the mud being precipitated out by described second-level settling pond.Described sterilization pool
Water inlet is connected with the outlet of described second-level settling pond, described second-level settling pond be vertical sedimentation basin,
Radical sedimentation basin or the one of rectangular sedimentation tank.Described Sedimentation tank, described oil interceptor, described anaerobic pond,
Described neutralization pond, described flotation tank, described first stage precipitation tank, described aerobic pond, described second-level settling pond with
And described sterilization pool is expoxy glass steel structure water pond, described sludge press filtration device is configured with Pulp pump.
The production method of the present embodiment comprises the following steps:
1) vegetable oil acid, hargil, lithium carbonate and water are added to polymeric kettle, carry out polyreaction；
2) will the product press-in acidifying still after polymerization be acidified；
3) by filter press, the product after acidifying is filtered, obtain rough dimeric dibasic acid；
4) will rough dimeric dibasic acid press-in transfer still be kept in；
5) rough dimeric dibasic acid is fed to centrifugal separating device, and mix with hot water, be centrifuged separating；
6), in the product feeding membrane evaporator after being performing centrifugal separation on, distill, remove steam；
7) product after membrane evaporator processes is fed to molecular distillation apparatus, separate；
8) the smart dimeric dibasic acid feeding pipeline switch filtering device obtained after separating enters surge tank and pre-mistake
Filter；
9) product press-in polycondensation vessel pre-filtering obtained, is simultaneously added dropwise ethylenediamine and carries out polycondensation reaction；
10) by defecator, the product after polycondensation reaction is filtered；
11) the product feeding prilling granulator after filtering carries out pelletize, obtains product.
Described step 1) the middle one that vegetable oil acid is behenic acid or cotton oil acid used, described vegetable oil acid,
The mass ratio of described hargil, described lithium carbonate and described water is 100:10:0.5:1.5；Described polymerization is anti-
The reaction temperature answered is 230 DEG C, and the response time of polyreaction is (3-4) h；
Described step 2) in use acidulant be phosphoric acid, described phosphoric acid and the product quality ratio after described polymerization
For 3:100；Reaction process is: acidificatoin time is 1h, and reaction temperature is (150-180) DEG C；
Described step 5) in add water temperature be (85-95) DEG C；
Described step 6) vapourizing temperature be 160 DEG C；
Described step 7) separation temperature be 230 DEG C, vacuum is below 30Pa；
Described step 9) in the mol ratio of dimeric dibasic acid after pre-filtering and ethylenediamine be 1:1, reaction includes following
Several stages:
8.1) the dimeric dibasic acid heating period, heating-up temperature is (125-133) DEG C；
8.2) the dropping stage of ethylenediamine, time for adding is (25-35) min；
8.3) intensification polycondensation phase, temperature rises to (190-205) DEG C；
8.4) the constant temperature stage, temperature controls as (215-225) DEG C；The isothermal reaction time is (3-4) h；
8.5) decompression phase, reduces pressure under 5mmHg.
The present embodiment, by vegetable oil acid, hargil, lithium carbonate and water being added to polymeric kettle 101, enters
Heavy metal ion in row polyreaction, and adsorption reaction thing, then by the product press-in acidifying still after polymerization
It is acidified；By filter press, the product after acidifying is filtered, obtain rough dimeric dibasic acid, by rough
Dimeric dibasic acid press-in transfer still is kept in.By rough dimeric dibasic acid is fed to centrifugal separating device, and
Mixing with hot water, be centrifuged separating, the product after being performing centrifugal separation on feeds membrane evaporator successively and divides
In sub-distilling apparatus, carry out distilling, separating, obtain smart dimeric dibasic acid.The smart dimeric dibasic acid feeding that will obtain after distillation
People's surge tank 702 and pre-filtering tank 704 is entered to pipeline switch filtering device；The product pressure that pre-filtering is obtained
Enter polycondensation vessel 801, be simultaneously added dropwise ethylenediamine and carry out polycondensation reaction；Again by defecator to after polycondensation reaction
Product filter；Product feeding prilling granulator after filtering carries out pelletize, obtains product.The present invention
The high temperature organic exhaust gas and the steam that membrane evaporator and molecular distillation apparatus are evaporated pass through high-temp waste gas
Processing means condenses, and collects, purifies, condensation in condensed waste liquid inflow waste collection tank 120182
Rear expellant gas together enters spray cleaning exhaust device with the organic exhaust gas that pelletize produces and carries out secondary purifying
Change, dedusting, then discharge after odor removal decomposes.The waste water produced in production all flows at waste water
Reason device processes.Concrete technology is as follows: first waste water carried out by the waste water produced in production through Sedimentation tank
Solid-liquid separation, then through described oil interceptor, waste water is carried out aqueous phase-separation of oil.Described oil interceptor is configured with draws water
Pump, described suction pump is by isolated waste water lifting to anaerobic pond.Organic in waste water of described anaerobic pond
Thing decomposes, and described neutralization pond is neutralized process, described flotation tank to the waste water after anaerobic pond processes
Bottom be provided with blowing device, described flotation tank by described blowing device by described flotation tank waste water
Particle blows to liquid level, and is carried by the waste water below superposed layer and precipitating into described first stage precipitation tank.Warp
Waste water after first stage precipitation tank precipitation flows into described aerobic pond, carries out nitration treatment；After aerobic pond processes
Waste water flows in second-level settling pond, again settles.Sludge press filtration device is in order to by described second-level settling pond
The mud being precipitated out carries out being dehydrated concentration.Waste water after second-level settling pond processes flows into described sterilization
Chi Zhong, after carrying out disinfection, discharges.
The foregoing is only the preferred embodiment of the invention, not in order to limit the invention,
Any amendment, equivalent and the improvement etc. made within all spirit in the invention and principle, all should
Within being included in the protection domain of the invention.
Claims (10)
1. a process units for smart dimeric dibasic acid, including membrane evaporator, molecular distillation apparatus, high-temp waste gas
Processing means and wastewater treatment equipment；Described high-temperature waste gas treating apparatus will evaporate through described membrane evaporator
The steam gone out and the isolated organic exhaust gas of described molecular distillation apparatus carry out condensation separation process, described useless
Water treatment facilities by essence dimeric dibasic acid production process in and high-temperature waste gas treating apparatus produce waste water purify
Process；Described wastewater treatment equipment include Sedimentation tank, oil interceptor, anaerobic pond, neutralization pond, flotation tank, one
Level sedimentation tank, aerobic pond and second-level settling pond；It is characterized in that: centrifugal separating device, described thin film steam
Send out device and described molecular distillation apparatus is set gradually from front to back by technological process；
Described centrifugal separating device includes centrifuge, separating tank and drain pipe；Described centrifuge include housing,
Upper cover, rotary drum, light phase weir, heavy phase weir；Described rotary drum is arranged on the center of described housing, described light phase
Weir is arranged on the open area at described rotary drum top, and described heavy phase weir is arranged on the bottom of described upper cover；Described
The 3rd charging aperture, the first water inlet, light phase export and heavy out is offered on housing；Described 3rd enters
Material mouth and described first water inlet are positioned at described light phase export and the lower section of described heavy out；Cover on described
Offering the first row mouth of a river, the described first row mouth of a river is docked mutually with described drain pipe, and described drain pipe is arranged
There is the second elevator pump；Described separating tank is arranged on the lower section of described heavy out, is provided with in described separating tank
Baffle plate, there is gap with the bottom of described separating tank inwall in the bottom of described baffle plate；
Described high-temperature waste gas treating apparatus includes ventilate tank, the second pipe bundle condenser, coil pipe and refrigerating plant；
The lower end of described ventilation tank offers air inlet；Described coil pipe is arranged on the inside of described ventilation tank in the shape of a spiral
In cavity, the bottom of described coil pipe is provided with water inlet, and the top of described coil pipe is provided with outlet, described
The water inlet of coil pipe and the outlet of described coil pipe all extend to outside the tank body of described ventilation tank；Described coil pipe
The discharge outlet of water inlet and described refrigerating plant interlink, the outlet of described coil pipe and described refrigerating plant
Water inlet interlink；Described second pipe bundle condenser is arranged on the top of described ventilation tank, described secondary series
The bottom of pipework condensation device is interlinked by the top of the second airway with described ventilation tank, and described second tubulation is cold
The top of condenser connects downtake pipe；
Described Sedimentation tank, oil interceptor, anaerobic pond, neutralization pond, flotation tank, first stage precipitation tank, aerobic pond with
And second-level settling pond is set gradually from front to back by technological process；Waste water is carried out solid-liquid separation by described Sedimentation tank,
Waste water is carried out aqueous phase-separation of oil by described oil interceptor；Described oil interceptor is configured with suction pump, described suction pump
By in isolated waste water lifting to anaerobic pond；Organic substance in waste water is decomposed by described anaerobic pond, institute
Stating neutralization pond and the waste water after anaerobic pond processes is neutralized process, the bottom of described flotation tank is provided with blows
Wind apparatus, the particle in described flotation tank waste water is blown to liquid by described blowing device by described flotation tank
Face, and the waste water below superposed layer is carried and precipitates into described first stage precipitation tank；Described aerobic pond is to inflow
Waste water therein carries out nitration treatment；Waste water therein for inflow is settled by described second-level settling pond again.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: described turn
Offering on the inwall of drum and be equipped with temperature control equipment, described temperature control equipment includes that temperature detector, electronics heat
Device and add heat pipe, the temperature test scope of described temperature detector is (50-100) DEG C.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: through described
Its temperature range of water that water inlet flows into is (85-95) DEG C.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: described gear
Plate is welded on the sidewall of described separating tank internal cavities, and described separating tank is divided into the first cavity and second
Cavity；Described gap is (1-5) cm.
The most according to claim 4 a kind of essence dimeric dibasic acid process units, it is characterised in that: described from
Heart segregation apparatus also includes heavy phase discharge pipe, and described heavy phase discharge pipe is provided with the 3rd elevator pump, described heavy
Phase discharge pipe one end be connected with described heavy out, the other end of described heavy phase discharge pipe extends to institute
Stating in the first cavity or extend in described second cavity, described heavy phase discharge pipe is connected with described heavy out；
Described separating tank is provided with band and stays the universal wheel of dynamic device.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: described logical
The bottom of gas tank is further opened with waste liquid outlet, and described high-temperature waste gas treating apparatus also includes waste collecting device；
Described waste collecting device includes that catheter and waste collection tank, the top of described waste collection tank pass through institute
State catheter to be connected with described ventilation tank.
The process units of a kind of essence dimeric dibasic acid the most according to claim 6, it is characterised in that: described useless
Be further opened with automatic draining device on liquid collecting tank, described automatic draining device include the second liquid level sensor with
And electronics lock, described second liquid level sensor is arranged on the inwall of described waste collection tank, described electronics lock
It is arranged at the leakage fluid dram of described waste collection tank.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: described the
Two pipe bundle condensers are provided with in the second deflection plate, described second deflection plate and described second pipe bundle condenser
Condensing tube be connected.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: described dish
The water side of pipe is additionally provided with the 6th and carries material pump.
The process units of a kind of essence dimeric dibasic acid the most according to claim 1, it is characterised in that: in described
With pond is provided with pH regulator instrument, described wastewater treatment equipment also includes sludge press filtration device and sterilization pool,
Described sludge press filtration device carries out being dehydrated concentration in order to the mud being precipitated out by described second-level settling pond；
The water inlet of described sterilization pool is connected with the outlet of described second-level settling pond, and described second-level settling pond is perpendicular
The one of flow settling pond, radical sedimentation basin or rectangular sedimentation tank；Described Sedimentation tank, described oil interceptor,
Described anaerobic pond, described neutralization pond, described flotation tank, described first stage precipitation tank, described aerobic pond, described
Second-level settling pond and described sterilization pool are expoxy glass steel structure water pond, and described sludge press filtration device configures
There is Pulp pump.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101492358A (en) * | 2009-03-07 | 2009-07-29 | 江西省宜春远大化工有限公司 | Method for producing low-phosphor dimer acid |
| CN101838193A (en) * | 2010-05-25 | 2010-09-22 | 九江力山环保科技有限公司 | Light-colored low-phosphorous dimer acid production process |
| CN201704238U (en) * | 2010-06-11 | 2011-01-12 | 九江力山环保科技有限公司 | Production equipment of dimer acid |
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2015
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101492358A (en) * | 2009-03-07 | 2009-07-29 | 江西省宜春远大化工有限公司 | Method for producing low-phosphor dimer acid |
| CN101838193A (en) * | 2010-05-25 | 2010-09-22 | 九江力山环保科技有限公司 | Light-colored low-phosphorous dimer acid production process |
| CN201704238U (en) * | 2010-06-11 | 2011-01-12 | 九江力山环保科技有限公司 | Production equipment of dimer acid |
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| Title |
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| 分子蒸馏技术用于制备高纯二聚脂肪酸的工艺研究;冯光炷等;《粮油加工与食品机械》;20051231(第11期);第53-56页 * |
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