CN111560036A - NBPT production facility - Google Patents
NBPT production facility Download PDFInfo
- Publication number
- CN111560036A CN111560036A CN202010405257.0A CN202010405257A CN111560036A CN 111560036 A CN111560036 A CN 111560036A CN 202010405257 A CN202010405257 A CN 202010405257A CN 111560036 A CN111560036 A CN 111560036A
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- Prior art keywords
- push plate
- barrel
- main
- bull stick
- rod
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 238000005406 washing Methods 0.000 claims abstract description 52
- 238000003756 stirring Methods 0.000 claims abstract description 50
- 238000004821 distillation Methods 0.000 claims abstract description 39
- 239000007788 liquid Substances 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000012074 organic phase Substances 0.000 claims abstract description 25
- 238000007789 sealing Methods 0.000 claims abstract description 19
- 239000012071 phase Substances 0.000 claims abstract description 16
- 230000007246 mechanism Effects 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims abstract description 8
- 244000309464 bull Species 0.000 claims description 28
- 230000000670 limiting effect Effects 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 5
- 230000008878 coupling Effects 0.000 claims description 5
- 238000010168 coupling process Methods 0.000 claims description 5
- 238000005859 coupling reaction Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 230000002441 reversible effect Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 7
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 22
- 238000005192 partition Methods 0.000 description 12
- 235000019270 ammonium chloride Nutrition 0.000 description 11
- 239000003960 organic solvent Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 9
- 239000008346 aqueous phase Substances 0.000 description 7
- 238000000926 separation method Methods 0.000 description 7
- HQABUPZFAYXKJW-UHFFFAOYSA-N butan-1-amine Chemical compound CCCCN HQABUPZFAYXKJW-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 108010046334 Urease Proteins 0.000 description 5
- 239000004202 carbamide Substances 0.000 description 5
- 230000002829 reductive effect Effects 0.000 description 5
- XSQUKJJJFZCRTK-UHFFFAOYSA-N urea group Chemical group NC(=O)N XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 239000003446 ligand Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- WQYSXVGEZYESBR-UHFFFAOYSA-N thiophosphoryl chloride Chemical compound ClP(Cl)(Cl)=S WQYSXVGEZYESBR-UHFFFAOYSA-N 0.000 description 4
- 241000883990 Flabellum Species 0.000 description 3
- 238000004176 ammonification Methods 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 2
- 235000017491 Bambusa tulda Nutrition 0.000 description 2
- 241001330002 Bambuseae Species 0.000 description 2
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000011425 bamboo Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 229940090496 Urease inhibitor Drugs 0.000 description 1
- -1 amino compound Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- KXDHJXZQYSOELW-UHFFFAOYSA-N carbonic acid monoamide Natural products NC(O)=O KXDHJXZQYSOELW-UHFFFAOYSA-N 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002815 nickel Chemical group 0.000 description 1
- 125000004433 nitrogen atom Chemical group N* 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 125000003003 spiro group Chemical group 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000002601 urease inhibitor Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/06—Phosphorus compounds without P—C bonds
- C07F9/22—Amides of acids of phosphorus
- C07F9/224—Phosphorus triamides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0446—Juxtaposition of mixers-settlers
- B01D11/0457—Juxtaposition of mixers-settlers comprising rotating mechanisms, e.g. mixers, mixing pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0488—Flow sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0492—Applications, solvents used
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention discloses NBPT production equipment, which comprises a micro heat exchanger, a micro mixer, a micro pipeline reactor, an ammoniation reactor, a water washing device, a distillation device, a crystallizing tank and a target dryer which are sequentially communicated, wherein the water washing device comprises a main washing barrel, a telescopic stirring paddle, a water washing motor, a secondary push plate and a main push plate, the secondary push plate and the main push plate can be embedded in an up-and-down sealing mode, a delayer and a water phase collector are connected onto a lower barrel, the lower end of the delayer is communicated with an organic phase outlet of the lower barrel, a connecting pipe is communicated with the water phase collector, a distillation main body of the distillation device comprises an upper cavity, an inner barrel, an outer barrel and a condenser, a stirring mechanism of the distillation device comprises a push rod, a distillation motor, a gear, a stirring rod and fan blades, and the fan blades move up. The invention avoids vortex influence caused by discharging below, improves the material liquid layering effect, realizes full stirring of the material liquid to be distilled at different heights in the inner cylinder body, and enables the material liquid to be distilled to be heated uniformly.
Description
Technical Field
The invention relates to the technical field of chemical production equipment, in particular to NBPT production equipment.
Background
N-N-butyl thiophosphoric triamide (NBPT) is a high-efficiency soil urease inhibitor, has an excellent urease inhibiting effect, can obviously reduce the decomposition of urea in soil and increase the utilization rate of nitrogen by crops. The inhibition mechanism is to compete for ligand and reduce the activity of urease, nitrogen atom in NBPT molecule and nickel atom in urease form (N-Ni) ligand, amino compound in the molecule and oxygen atom in carbamic acid bridge can form tridentate ligand which is firmer than monodentate ligand formed by urea and urease, so that the contact between urea and urease is reduced, the hydrolysis speed of urea is slowed down, and the utilization rate of urea is improved. The currently adopted method for synthesizing N-N-butyl thiophosphoric triamide by continuous reaction comprises the following steps: (1) mixing thiophosphoryl chloride and an organic solvent, precooling the mixture to-5-0 ℃ in a micro heat exchanger, then mixing the mixture with N-butylamine and an inorganic alkaline aqueous solution which are precooled to-5-0 ℃ in a micro mixer, and reacting the obtained mixture in a multi-section series micro-pipeline reactor to obtain N-N-butyl thiophosphoryl dichloride; (2) directly feeding N-N-butyl thiophosphoryl dichloride into an ammoniation reactor to carry out ammoniation reaction with ammonia gas, washing, layering and filtering after the ammoniation reaction is completed, decompressing and distilling filtrate to recover solvent, crystallizing and drying to obtain the N-N-butyl thiophosphoryl triamide. Because the prior equipment for producing the N-N-butyl thiophosphoric triamide still has the defects of low separation precision, unsatisfactory purity of final products, large consumption of raw materials and the like, if the traditional washing device is adopted to separate the reaction by-product ammonium chloride, the layered feed liquid is discharged and collected from the lower part, vortex appears near the liquid outlet in the discharging process, in addition, when organic phase is separated, the water phase layer and the organic phase layer of the material liquid are difficult to be accurately controlled and separated, a small part of the water phase layer can be separated out always, the separation effect of the material liquid is influenced, and if a traditional reduced pressure distillation device is adopted for separating organic solvent, because the stirring mechanism rotates from one direction only and the stirring is not uniform enough, the organic solvent is easily heated unevenly, the reduced pressure distillation extraction rate is low, therefore, the development and design of N-N-butyl thiophosphoric triamide production equipment with good separation effect and high vacuum distillation extraction rate has important industrial value.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide NBPT production equipment, which avoids vortex influence caused by discharging below, improves the material liquid layering effect, realizes high-purity accurate separation of ammonium chloride, realizes full stirring of material liquids to be distilled at different heights in an inner cylinder body, enables the material liquids to be distilled to be uniformly heated, and improves the purity of the final NBPT.
In order to achieve the purpose, the invention adopts the following technical scheme:
the NBPT production equipment comprises a micro heat exchanger, a micro mixer, a micro pipeline reactor, an ammonification reactor, a washing device, a distillation device, a crystallizing tank and a target dryer which are sequentially communicated, wherein the washing device comprises a main washing barrel, a telescopic stirring paddle arranged in the main washing barrel, a washing motor used for driving the telescopic stirring paddle to rotate, a secondary push plate and a main push plate which are arranged from top to bottom, the main washing barrel comprises a lower barrel body, the secondary push plate and the main push plate are respectively arranged in the lower barrel body in a sliding manner, a liquid inlet communicated with the ammonification reactor is arranged on the lower barrel body and positioned above the secondary push plate, air cylinders used for driving the main push plate to move are respectively arranged on two sides of the main washing barrel, the secondary push plate and the main push plate are respectively embedded in a sealing manner from top to bottom between the secondary push plate and the main push plate under the action of the tensile force of the air cylinders and the weight of liquid injected into the space above the secondary push plate, one side of the upper end of the lower barrel body is respectively, the lower barrel bottom is equipped with the organic phase export, the delayer lower extreme passes through connecting pipe and organic phase export intercommunication, the connecting pipe passes through branch pipe and water phase collector intercommunication, distillation plant includes distillation main part and rabbling mechanism, the distillation main part includes the cavity, is located the interior barrel and the outer barrel that set up in cavity below and inside and outside, with the condenser of interior barrel upper portion intercommunication, rabbling mechanism includes push rod, the horizontal reciprocating motion's of drive push rod distillation motor, drives just reversing cross moving gear, fixes under the gear terminal surface and stretch into the puddler of interior barrel and with the flabellum of puddler lower part spiro union, the flabellum is along with just reversing cross moving and up-and-down motion of puddler.
The main section of thick bamboo of washing still includes the baffle that can dismantle the connection, the main section of thick bamboo of washing is separated into the last barrel and the lower barrel that sets up from top to bottom by the baffle, flexible stirring rake includes with the first bull stick of the pivot rigid coupling of washing motor, slide and inlay and establish in first bull stick and can follow first bull stick pivoted second bull stick, slide and inlay and establish in the second bull stick and can follow second bull stick pivoted third bull stick and the stirring leaf of rigid coupling in the third bull stick bottom, first bull stick lower extreme passes the baffle and is connected with the baffle rotation through A bearing, pass through spring coupling between the pivot of washing motor and the interior terminal surface of third bull stick lower part.
The outside horizontal extension in second bull stick upper end forms the fixture block that a pair of symmetry set up, the sunken a pair of draw-in groove that forms of first bull stick up end, the fixture block card is gone into in the draw-in groove and can slide from top to bottom along the draw-in groove, the outside horizontal extension in third bull stick upper end forms the lug that a pair of symmetry set up, the sunken a pair of recess that forms of second bull stick up end, the lug card is gone into in the recess and can slide from top to bottom along the recess.
The lower barrel is provided with a limiting block with uniform circumference on the inner wall of the lower portion, the secondary push plate is arranged in the lower barrel and located above the limiting block, and the main push plate is provided with a notch through which the limiting block can pass.
Inferior push pedal is last by interior and be equipped with a plurality of through-holes that circle outward, main push pedal includes through-hole and a plurality of circles down and be used for the boss of through-hole in the shutoff, every circle the through-hole sets up between adjacent two circles of boss down, is located through-hole terminal surface outlying inlay and be equipped with the A sealing washer in inferior push pedal, it is sealed through the A sealing washer when through-hole in the boss embedding shutoff.
A rotating rod is connected to a rotating shaft of the distillation motor, and the outer end of the rotating rod drives a push rod to reciprocate through a fastener.
The push rod comprises a toothed rod part engaged with the gear and a slide rod part vertically connected with the toothed rod part, the toothed rod part and the slide rod part form a T-shaped structure, a pair of fixing parts for the toothed rod part to slide through are fixedly arranged on the upper portion of the upper chamber, a waist hole is formed in the slide rod part along the length direction of the slide rod part, and the fastening parts penetrate through the waist hole and are in sliding connection with the waist hole.
The heating wire is fixedly arranged on the annular outer wall of the inner cylinder body, and a wire mesh demister is arranged in the upper space of the inner cylinder body.
One side of the bottom of the inner cylinder body is provided with a feed inlet communicated with the organic phase outlet, and the other side of the bottom of the inner cylinder body is provided with a discharge outlet communicated with the crystallizing tank.
The invention has the beneficial effects that: stirring the reaction solution by a telescopic stirring paddle to accelerate the dissolution of ammonium chloride; the secondary push plate and the main push plate are pulled by the air cylinder to move upwards, and the water phase layer and the interface layer of the standing and layered material liquid overflow upwards respectively and are discharged to the water phase collector and the delayer, so that the vortex influence caused by discharging below is avoided, the material liquid layering effect is improved, and the high-purity accurate separation of ammonium chloride is realized; the interface layer is rested and layered into a water phase layer and an organic phase layer through the delayer, so that the separation precision of ammonium chloride is further improved, and the improvement of the final purity of NBPT is facilitated; make the puddler can just reverse cross operation through the mating reaction of distillation motor, push rod, gear for the flabellum up-and-down motion and then realize treating the intensive mixing of distillation feed liquid to the internal co-altitude of inner tube, make and treat that the distillation feed liquid is heated evenly, improve the distillation pull-out rate, further promote final NBPT's purity.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic front view of the washing apparatus of the present invention;
FIG. 3 is an enlarged view taken at A in FIG. 2;
FIG. 4 is an enlarged view at B in FIG. 2;
FIG. 5 is an enlarged view at C of FIG. 2;
FIG. 6 is an enlarged view taken at D in FIG. 2;
FIG. 7 is a schematic side view of the washing apparatus of the present invention;
FIG. 8 is a schematic top view of a secondary push plate of the present invention;
FIG. 9 is a schematic top view of the main push plate of the present invention;
FIG. 10 is a schematic view of the structure of a distillation apparatus according to the present invention;
FIG. 11 is an enlarged view at E in FIG. 10;
FIG. 12 is an enlarged view at F of FIG. 10;
FIG. 13 is an enlarged view at G of FIG. 10;
FIG. 14 is a top schematic view of a push rod mounting arrangement embodying the principles of the present invention;
FIG. 15 is an enlarged view at H in FIG. 14;
fig. 16 is an enlarged view at I in fig. 14.
In the figure: the micro heat exchanger 1, the micro mixer 2, the micro pipeline reactor 3, the ammoniation reactor 4, the water washing device 5, the main washing cylinder 51, the upper cylinder 511, the lower cylinder 512, the liquid inlet 513, the organic phase outlet 514, the partition 515, the A bearing 516, the B bearing 517, the limit block 518, the notch 519, the telescopic stirring paddle 52, the first rotating rod 521, the second rotating rod 522, the third rotating rod 523, the stirring blade 524, the clamping groove 525, the clamping block 526, the groove 527, the bump 528, the spring 529, the water washing motor 53, the secondary push plate 54, the upper through hole 541, the A sealing ring 542, the B sealing ring 543, the main push plate 55, the boss 551, the lower through hole 552, the delayer 56, the aqueous phase collector 57, the cylinder 58, the connecting rod 581, the connecting pipe 59, the branch pipe 591, the distillation device 6, the distillation body 61, the upper chamber 611, the inner cylinder 612, the outer cylinder 613, the feeding hole 614, the discharging hole 615, the end cover 616, the push rod 62, The device comprises a waist hole 623, a fixing piece 624, a distillation motor 63, a rotary rod 631, a fastening piece 632, a gear 64, a fixing rod 641, a stirring rod 65, a fan blade 66, a condenser 67, a heating wire 68, a wire mesh demister 69, a crystallizing tank 7 and a target dryer 8.
Detailed Description
The invention is further described with reference to the accompanying drawings and the detailed description below:
as shown in figures 1-16, an NBPT production device comprises a micro heat exchanger 1, a micro mixer 2, a micro pipeline reactor 3, an ammoniation reactor 4, a water washing device 5, a distillation device 6, a crystallization tank 7 and a target dryer 8 which are sequentially communicated, wherein the micro heat exchanger 1 is used for precooling mixed thiophosphoryl chloride and an organic solvent to-5-0 ℃, the micro mixer 2 is used for fully mixing the thiophosphoryl chloride and the organic solvent precooled to-5-0 ℃ with N-butylamine and an inorganic alkaline water solution precooled to-5-0 ℃, the micro pipeline reactor 3 is used for reacting the thiophosphoryl chloride and the N-butylamine to generate N-N-butyl thiophosphoryl dichloride, the ammoniation reactor 4 is used for reacting the N-N-butyl thiophosphoryl dichloride and ammonia gas to generate NBPT and a byproduct ammonium chloride, and the water washing device 5 is mainly used for washing the product generated by the reaction, Standing for layering to separate out a byproduct ammonium chloride, wherein the distillation device 6 is used for removing organic solvent remained in a product, the crystallization tank 7 is used for carrying out crystallization treatment on NBPT obtained after reduced pressure distillation, and the target dryer 8 is used for drying the crystallized NBPT.
The micro heat exchanger 1, the micro mixer 2, the micro pipeline reactor 3, the ammonification reactor 4, the crystallization tank 7 and the target dryer 8 are common devices in the field of chemical equipment, and are not described in detail herein.
The washing device 5 comprises a main washing barrel 51, a telescopic stirring paddle 52 arranged in the main washing barrel 51, a washing motor 53 used for driving the telescopic stirring paddle 52 to rotate, a secondary push plate 54 and a main push plate 55 arranged from top to bottom, wherein the main washing barrel 51 comprises a lower barrel 512, the secondary push plate 54 and the main push plate 55 are respectively arranged in the lower barrel 512 in a sliding manner, a liquid inlet 513 communicated with the ammoniation reactor 4 is arranged on the lower barrel 512 above the secondary push plate 54, two sides of the main washing barrel 51 are respectively provided with a cylinder 58 used for driving the main push plate 55 to move, the secondary push plate 54 and the main push plate 55 realize the upper and lower sealing embedding between the secondary push plate 54 and the main push plate 55 under the action of the pulling force of the cylinder 58 and the weight of liquid injected into the space above the secondary push plate 54, one side of the upper end of the lower barrel 512 is respectively connected with a delayer 56 and a water phase collector 57 which are both communicated with the lower barrel 512, the bottom of the lower barrel 512 is provided with, the lower end of the delaminator 56 communicates with the organic phase outlet 514 through a connection pipe 59, and the connection pipe 59 communicates with the aqueous phase collector 57 through a branch pipe 591. The liquid inlet 513 is located above the initial position of the secondary push plate 54, so that the liquid enters the sealed space after the space above the secondary push plate 54 forms the sealed space. The delayer 56 is a longitudinally arranged structure with a smaller inner diameter and is used for delaminating the interface phase layer (the interface between the water phase layer and the organic phase layer is the interface phase layer) again, the water phase collector 57 is connected to the upper part of the lower cylinder 512, the delayer 56 is connected to the upper part of the lower cylinder 512, the lower end of the delayer 56 is connected to the connecting pipe 59, the connecting pipe 59 is connected to the organic phase outlet 514, and the branch pipe 591 is connected to the connecting pipe 59 and is provided with a valve for controlling liquid outflow.
The main washing cylinder 51 further comprises a partition plate 515 which is detachably connected, the upper end cover part of the main washing cylinder 51 is also detachably arranged, so that the telescopic stirring paddle 52, the connecting rod 581, the secondary push plate 54 and the main push plate 55 can be conveniently installed, the main washing cylinder 51 is divided into an upper cylinder 511 and a lower cylinder 512 which are vertically arranged by the partition plate 515, and the upper end surface of the lower cylinder 512 is further provided with an organic solvent inlet and a distilled water inlet.
A rotating shaft of the washing motor 53 penetrates through the upper end of the upper cylinder 511 and is rotatably connected with the upper end of the upper cylinder 511 through a B bearing 517, the telescopic stirring paddle 52 comprises a first rotating rod 521 fixedly connected with the rotating shaft of the washing motor 53, a second rotating rod 522 slidably embedded in the first rotating rod 521 and capable of rotating along with the first rotating rod 521, a third rotating rod 523 slidably embedded in the second rotating rod 522 and capable of rotating along with the second rotating rod 522, and a stirring blade 524 fixedly connected to the bottom end of the third rotating rod 523, the lower end of the first rotating rod 521 passes through the partition 515 and is rotatably connected with the partition 515 through an a bearing 516, the rotating shaft of the washing motor 53 is connected with the inner end surface of the lower part of the third rotating rod 523 through a spring 529, and the spring 529 plays a role in further stably connecting the first rotating rod 521, the second rotating rod 522 and the third rotating rod 523 on one hand, and enables the telescopic stirring paddle 52 to automatically recover to an extension state after being compressed on the other hand.
The specific connection structure among the first rotating rod 521, the second rotating rod 522 and the third rotating rod 523 is as follows: the upper end of the second rotating rod 522 extends outwards horizontally to form a pair of symmetrically-arranged clamping blocks 526, the upper end surface of the first rotating rod 521 is recessed to form a pair of clamping grooves 525, the clamping grooves 525 do not penetrate through the first rotating rod 521, the clamping blocks 526 are clamped in the clamping grooves 525 and can slide up and down along the clamping grooves 525, the upper end of the third rotating rod 523 extends outwards horizontally to form a pair of symmetrically-arranged lugs 528, the upper end surface of the second rotating rod 522 is recessed to form a pair of grooves 527, the grooves 527 do not penetrate through the second rotating rod 522, and the lugs 528 are clamped in the grooves 527 and can slide up and down along the grooves 527; the lower opening of the first rotating rod 521 is sealed with the annular outer wall of the second rotating rod 522 through a sealing ring embedded in the annular inner wall of the lower opening of the first rotating rod 521, the lower opening of the second rotating rod 522 is sealed with the annular outer wall of the third rotating rod 523 through a sealing ring embedded in the annular inner wall of the lower opening of the second rotating rod 522, the influence of feed liquid entering the telescopic stirring paddle 52 on the stirring and dissolving of ammonium chloride is avoided, and the loss of products is reduced.
The cylinder 58 is fixedly connected with the main push plate 55 through a right-angle connecting rod 581, the connecting rod 581 penetrates through the partition plate 515 and the secondary push plate 54, the connecting rod 581 and the partition plate 515 are sealed through a sealing ring embedded on the partition plate 515, and the connecting rod 581 and the partition plate 515 and the secondary push plate 54 are sealed through a sealing ring embedded in the secondary push plate 54, so that a closed space can be formed between the partition plate 515 and the secondary push plate 54.
The inner wall of the lower part of the lower cylinder 512 is provided with limit blocks 518 which are uniformly distributed on the circumference, the secondary push plate 54 is arranged in the lower cylinder 512 and is positioned above the limit blocks 518, the main push plate 55 is provided with a notch 519 which can enable the limit blocks 518 to pass through, the initial position of the secondary push plate 54 is limited by the arrangement of the limit blocks 518, the downward movement of the secondary push plate 54 is prevented, and the main push plate 55 can be separated from the secondary push plate 54 so that the organic phase can flow downwards to the organic phase outlet 514 and be discharged.
The secondary push plate 54 is provided with a plurality of upper through holes 541 from inside to outside, the main push plate 55 comprises a plurality of circles of lower through holes 552 and a plurality of circles of bosses 551 for plugging the upper through holes 541, each circle of the lower through holes 552 is arranged between two adjacent circles of the bosses 551, the secondary push plate 54 positioned on the periphery of the lower end surface of the upper through holes 541 is embedded with an A sealing ring 542, and the bosses 551 are sealed by the A sealing ring 542 when being embedded into the upper through holes 61. The upper through hole 541 is a tapered hole with a small upper part and a large lower part, the boss 551 is a tapered circular truncated cone structure with a small upper part and a large lower part, and the space between the annular outer wall of the secondary push plate 54 and the annular inner wall of the lower barrel 512 is sealed by a B sealing ring 543 embedded on the secondary push plate 54. Through the structural design, a closed space can be formed between the partition plate 515 and the secondary push plate 54, and the purpose of upwards extruding and discharging the liquid of the aqueous phase layer and the interface layer is further realized.
The water washing device 5 is mainly used for washing and standing the product after the reaction is finished to separate an ammonium chloride by-product. The working principle of the water washing device 5 is as follows: in an initial state, the secondary push plate 54 and the main push plate 55 are in a separated state, the starting air cylinder 58 drives the main push plate 55 to move upwards to enable the boss 551 to be embedded into the upper through hole 541, the operation of the air cylinder 58 is stopped, a small part of organic solvent is injected into the lower barrel 512, at the moment, under the combined action of the gravity of the organic solvent and the pulling force of the air cylinder 58, the main push plate 55 and the secondary push plate 54 are completely embedded in a sealing manner, the injection of the organic solvent is stopped, a product obtained after the reaction of the ammoniation reactor 4 is injected, distilled water is simultaneously injected, the washing motor 53 is started to stir, so that ammonium chloride is fully dissolved in the distilled water, the stirring is stopped, standing and layering are carried out, an aqueous phase layer (ammonium chloride aqueous solution), an interface layer and an organic phase layer (NBPT and organic solvent) distributed from top to bottom are obtained, the air cylinder 58 is started, a valve at the joint of the aqueous phase collector 57, closing a valve at the joint of the water phase collector 57 and the lower cylinder 512, opening a valve at the joint of the delayer 56 and the lower cylinder 512, discharging the interface layer to the delayer 56, wherein the telescopic stirring paddle 52 is compressed under the thrust of the secondary push plate 54, the spring 529 is gradually compressed, the interface layer is layered again after the standing of the delayer 56 to form an organic phase layer and an organic phase layer, the obtained organic phase layer is discharged to the organic phase outlet 514, the aqueous phase layer is discharged to the aqueous phase collector 57, the cylinder 58 is started again to move the main push plate 55 downwards, the residual organic phase layer in the lower cylinder 512 gradually falls under the self gravity, and the secondary push plate 54 also gradually falls, in the process, the secondary push plate 54 and the main push plate 55 are still in a sealing embedded state, when the secondary push plate 54 moves downwards and abuts against the limiting block 518, the secondary push plate 54 does not move downwards, the main push plate 55 continues to move downwards and separates from the secondary push plate 54, the organic phase layer in the lower cylinder 512 passes through the upper through hole 541, the upper, The lower through hole 552 flows to the organic phase outlet 514, so that the precise separation of the liquid material is completed, and the retractable stirring paddle 52 is restored to the initial extension state under the action of gravity and the elastic force of the spring 529.
The distillation device 6 comprises a distillation main body 61 and a stirring mechanism, wherein the distillation main body 61 comprises an upper cavity 611, an inner cylinder 612 and an outer cylinder 613 which are arranged below and inside and outside the upper cavity 611, and a condenser 67 communicated with the upper part of the inner cylinder 612, a heating wire 68 is fixedly arranged on the annular outer wall of the inner cylinder 612 and used for heating liquid in the inner cylinder 612, and a wire mesh demister 69 is arranged in the upper space of the inner cylinder 612 and used for eliminating foam carried in evaporated gas, so that the problem that the foam enters the condenser 67 to be crystallized to cause the wall bonding of a heat exchange tube of the condenser 67 and influence the distillation effect is avoided.
The stirring mechanism comprises a push rod 62, a distillation motor 63 for driving the push rod 62 to transversely reciprocate, a gear 64 for driving the push rod 62 to rotate forward and backward in a crossed mode, a stirring rod 65 fixed on the lower end face of the gear 64 and extending into the inner cylinder 612, and fan blades 66 in threaded connection with the lower portion of the stirring rod 65, wherein the fan blades 66 move up and down along with the forward and backward rotation of the stirring rod 65 in a crossed mode. The upper chamber 611 comprises a detachably connected end cover 616, which facilitates the installation of the relevant components of the upper chamber 611, the gear 64 is fixed to the end cover 616 by a fixing rod 641, and the gear 64 and the fixing rod 641 are rotatably connected by a bearing; the stirring rod 65 is rotatably connected with the partition board which separates the upper chamber 611 and the inner cylinder 612 and the bottom of the stirring rod 65 and the bottom of the inner cylinder 612 through bearings, so that smooth rotation of the stirring rod 65 is ensured.
A rotating rod 631 is connected to the rotating shaft of the distillation motor 63, and the outer end of the rotating rod 631 drives the push rod 62 to reciprocate through a fastener 632.
The push rod 62 comprises a toothed rod portion 621 meshed with the gear 64 and a sliding rod portion 622 perpendicularly connected with the toothed rod portion 621, the toothed rod portion 621 and the sliding rod portion 622 form a T-shaped structure, a pair of fixing pieces 624 for the toothed rod portion 621 to slide through is fixedly arranged at the upper portion of the upper chamber 611, a waist hole 623 is arranged on the sliding rod portion 622 along the length direction of the sliding rod portion, and the fastening piece 632 penetrates through the waist hole 623 and is in sliding connection with the waist hole 623.
And a feed inlet 614 communicated with the organic phase outlet 514 is formed in one side of the bottom of the inner cylinder body 612, and a discharge outlet 615 communicated with the crystallizing tank 7 is formed in the other side of the bottom of the inner cylinder body 612.
The operating principle of the stirring mechanism is as follows: with reference to fig. 14 as a reference direction, the distillation motor 63 is started, the distillation motor 63 drives the rotary rod 631 to rotate circularly on a horizontal plane, the rotary rod 631 drives the fastener 632 to slide in the waist hole 623, when the fastener 632 slides clockwise by 180 degrees, the push rod 62 moves rightward to drive the gear 64 to rotate clockwise, the gear 64 drives the stirring rod 65 to rotate clockwise to further move the fan blade 66 upward, when the fastener 632 continues to slide clockwise by 180 degrees, the push rod 62 moves leftward to drive the gear 64 to rotate counterclockwise, and the gear 64 drives the stirring rod 65 to rotate counterclockwise to further move the fan blade 66 downward; the reciprocating motion realizes the up-and-down stirring of the liquid in the inner cylinder body 612, so that the stirring is more sufficient, the distilled liquid is uniformly heated, and the distillation extraction rate is improved.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (9)
1. The utility model provides a NBPT production facility, includes micro heat exchanger (1), micro mixer (2), micro pipeline reactor (3), ammoniation reactor (4), washing unit (5), distillation plant (6), crystallizer (7) and target dryer (8) that communicate in proper order, its characterized in that: the washing device (5) comprises a main washing cylinder (51), a telescopic stirring paddle (52) arranged in the main washing cylinder (51), a washing motor (53) used for driving the telescopic stirring paddle (52) to rotate, a secondary push plate (54) and a main push plate (55) which are arranged from top to bottom, wherein the main washing cylinder (51) comprises a lower cylinder body (512), the secondary push plate (54) and the main push plate (55) are respectively arranged in the lower cylinder body (512) in a sliding manner, a liquid inlet (513) communicated with the ammoniation reactor (4) is arranged on the lower cylinder body (512) above the secondary push plate (54), two sides of the main washing cylinder (51) are respectively provided with a cylinder (58) used for driving the main push plate (55) to move, the secondary push plate (54) and the main push plate (55) are in a sealing embedded manner from top to bottom between the secondary push plate (54) and the main push plate (55) under the action of the tensile force of the cylinder (58) and the liquid weight injected into the space above the secondary push plate (54), the device comprises a lower barrel (512), a delayer (56) and a water phase collector (57) which are communicated with the lower barrel (512) are connected to one side of the upper end of the lower barrel (512) respectively, an organic phase outlet (514) is arranged at the bottom of the lower barrel (512), the lower end of the delayer (56) is communicated with the organic phase outlet (514) through a connecting pipe (59), the connecting pipe (59) is communicated with the water phase collector (57) through a branch pipe (591), a distillation device (6) comprises a distillation main body (61) and a stirring mechanism, the distillation main body (61) comprises an upper chamber (611), an inner barrel (612) and an outer barrel (613) which are arranged below and inside and outside the upper chamber (611), and a condenser (67) communicated with the upper part of the inner barrel (612), the stirring mechanism comprises a push rod (62), a distillation motor (63) driving the push rod (62) to do transverse reciprocating motion, and gears (64) driving the forward and reverse rotation to, The stirring rod (65) is fixed on the lower end face of the gear (64) and extends into the inner cylinder (612), and the fan blades (66) are in threaded connection with the lower portion of the stirring rod (65), and the fan blades (66) move up and down along with the forward and reverse rotation cross operation of the stirring rod (65).
2. The NBPT production apparatus of claim 1, wherein: the main barrel (51) of washing still includes baffle (515) of dismantling the connection, main barrel (51) are separated into upper and lower barrel (511) and lower barrel (512) that set up by baffle (515) of washing, flexible stirring rake (52) include with the first bull stick (521) of the pivot rigid coupling of washing motor (53), slide and inlay and establish in first bull stick (521) and can follow first bull stick (521) pivoted second bull stick (522), slide and inlay and establish in second bull stick (522) and can follow second bull stick (522) pivoted third bull stick (523) and rigid coupling stirring leaf (524) in third bull stick (523) bottom, baffle (515) are passed through to first bull stick (521) lower extreme and are connected with baffle (515) rotation through A bearing (516), the pivot of washing motor (53) is connected through spring (529) between the interior terminal surface of third bull stick (523) lower part.
3. The NBPT production apparatus of claim 2, wherein: the outside horizontal extension in second bull stick (522) upper end forms fixture block (526) that a pair of symmetry set up, the terminal surface is sunken to form a pair of draw-in groove (525) on first bull stick (521), fixture block (526) are gone into in draw-in groove (525) and can slide from top to bottom along draw-in groove (525), the outside horizontal extension in third bull stick (523) upper end forms lug (528) that a pair of symmetry set up, the terminal surface is sunken to form a pair of recess (527) on second bull stick (522), lug (528) are gone into in recess (527) and can slide from top to bottom along recess (527).
4. The NBPT production apparatus of claim 2, wherein: the lower barrel (512) is provided with limiting blocks (518) which are uniformly distributed on the circumference on the inner wall of the lower portion of the lower barrel (512), the secondary push plate (54) is arranged in the lower barrel (512) and is positioned above the limiting blocks (518), and the main push plate (55) is provided with a notch (519) through which the limiting blocks (518) can pass.
5. The NBPT production apparatus of claim 1, wherein: the secondary push plate (54) is provided with a plurality of upper through holes (541) from inside to outside, the main push plate (55) comprises a plurality of lower through holes (552) and a plurality of bosses (551) for plugging the upper through holes (541), each lower through hole (552) is arranged between two adjacent bosses (551), an A sealing ring (542) is embedded on the secondary push plate (54) which is positioned at the periphery of the lower end face of the upper through hole (541), and the bosses (551) are sealed by the A sealing ring (542) when being embedded into and plugged into the upper through holes (61).
6. The NBPT production apparatus of claim 1, wherein: a rotating rod (631) is connected to a rotating shaft of the distillation motor (63), and the outer end of the rotating rod (631) drives the push rod (62) to reciprocate through a fastener (632).
7. The NBPT production apparatus of claim 6, wherein: the push rod (62) comprises a toothed rod part (621) meshed with the gear (64) and a sliding rod part (622) vertically connected with the toothed rod part (621), the toothed rod part (621) and the sliding rod part (622) form a T-shaped structure, a pair of fixing parts (624) for the toothed rod part (621) to slide through are fixedly arranged at the upper part of the upper cavity (611), a waist hole (623) arranged along the length direction of the sliding rod part (622) is arranged on the sliding rod part, and the fastening part (632) penetrates through the waist hole (623) and is in sliding connection with the waist hole (623).
8. The NBPT production apparatus of claim 1, wherein: the heating wire (68) is fixedly arranged on the annular outer wall of the inner cylinder body (612), and a wire mesh demister (69) is arranged in the upper space of the inner cylinder body (612).
9. The NBPT production apparatus of claim 1, wherein: and a feeding hole (614) communicated with the organic phase outlet (514) is formed in one side of the bottom of the inner cylinder body (612), and a discharging hole (615) communicated with the crystallizing tank (7) is formed in the other side of the bottom of the inner cylinder body (612).
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