CN103073592B - A kind of reaction unit for hermetically sealed production methylpyridine phosphorus - Google Patents
A kind of reaction unit for hermetically sealed production methylpyridine phosphorus Download PDFInfo
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- CN103073592B CN103073592B CN201210596227.8A CN201210596227A CN103073592B CN 103073592 B CN103073592 B CN 103073592B CN 201210596227 A CN201210596227 A CN 201210596227A CN 103073592 B CN103073592 B CN 103073592B
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Abstract
The invention provides a kind of reaction unit for hermetically sealed production methylpyridine phosphorus, it comprises one first reaction member, one second reaction member and one the 3rd reaction member.This first reaction member comprises an eddy flow still, an oxazole [4,5-b] pyridine-2 (3H) ketone storage tank, a DMF storage tank, a paraformaldehyde storage tank and monochlor(in)ate sulfoxide storage tank.Described first reaction member comprises one first powder liquid mixing pump, and described first powder liquid mixing pump comprises one first import and one first outlet.Described oxazole [4,5-b] pyridine-2 (3H) ketone storage tank, DMF storage tank and paraformaldehyde storage tank and described first inlet communication, described first outlet is communicated with described eddy flow still.Described eddy flow still comprises a first noumenon, and described the first noumenon hollow arranges formation one first reaction chamber, and described first reaction chamber is the conical structure of a handstand.Reaction unit provided by the invention, fundamentally can stop poisonous gas leakage, be conducive to environment protection.
Description
Technical field
The present invention relates to a kind of equipment for the production of methylpyridine phosphorus, particularly a kind of can the reaction unit of hermetically sealed production methylpyridine phosphorus.
Background technology
Methylpyridine phosphorus has another name called first base pyrrole Evil phosphorus, is a kind of excellent sterilant, and chemistry S-[the chloro-oxazole of 6-(4,5-b) pyridine-2 (3 hydrogen)-one base-methyl]-O, O-dimethyl sulphide substituted phosphate by name, molecular formula is C
9h
10clN
2o
5pS, molecular weight is in order to 324.68.Methylpyridine phosphorus is a kind of excellent miticide, have insecticidal activity concurrently, belong to and tagging and stomach toxicity medicament, long-lasting is good, insecticidal spectrum is wide, can be used for cotton, fruit tree, vegetables and livestock, public health and family, prevent and treat various mite class and stupid, aphid, leaf lice, small kernel-eating insect, colorado potato bug and fly, cockroach etc., this agent is to people and animals' low toxicity, belong to efficient, low toxicity, low residue resistant medicament, therefore methylpyridine phosphorus becomes the organic phosphorous insecticide of the World Health Organization (WHO) recommendation.Again because make emulsion, sprays, pulvis, wettable powder and sol particle in this methylpyridine phosphorus, be therefore specially adapted to the insects such as control fly.
Conventional picoline production of phosphorus mainly comprises three steps: step one, with oxazole [4,5-b] pyridine-2 (3H) ketone is raw material, then generates a kind of intermediate side chain chloro-product of methylpyridine phosphorus through nucleophilic chloro, methylolation; Step 2, with dimethylphosphite and sulfur reaction, under the effect of sodium methylate, generates the another kind of intermediate thiophosphatephosphorothioate of methylpyridine phosphorus; Step 3, finally by side chain chloro-product and thiophosphoric acid ester condensation reaction further synthesizing methyl pyridine phosphorus.Please refer to Fig. 1, is the module diagram of the device of the described methylpyridine phosphorus of existing production, and described device comprises the first reaction member 100, second reaction member 200, and the 3rd reaction member 300 be connected with first, second reaction member 100,200 described.At described first reaction member 100 for the production of intermediate product side chain chloro-product.Second reaction member 200 is for the production of intermediate product thiophosphatephosphorothioate.Above-mentioned two kinds of intermediate products and side chain chloro-product and thiophosphatephosphorothioate finally enter the 3rd reaction member 300, produce the finished product methylpyridine phosphorus.
Refer to Fig. 2, for the structural representation of traditional first reaction member 100, described first reaction member 100 comprises one first reactor 10, multiple the first storage tank 20, gas-holder 30 of communicating with this first reactor 10 and waste gas recovery tank 40 and one first whipping appts 50.Described first storage tank 20 comprises an oxazole [4,5-b] pyridine-2 (3H) ketone storage tank 21, DMF (DMF) storage tank 22, paraformaldehyde storage tank 23 and monochlor(in)ate sulfoxide storage tank 24.Described gas-holder 30 stores chlorine, when reacting, by a ventpipe (not shown), gas is imported the first reactor 10.40, described waste gas recovery tank reclaims by the recovery tube (not shown) extend in the first reactor 10 waste gas reacting and produce.Described first whipping appts 50 comprises the first stirring rod 51 extended in the first reactor 10.When reacting, the raw materials such as oxazole pyridone, DMF, paraformaldehyde and sulfur oxychloride being added the first reactor 10 according to a graded, and passes into chlorine, reacting while stirring.Referring to Fig. 3, is the structural representation of traditional second reaction member 200, and described second reaction member 200 comprises one second reactor 210, multiple the second storage tank 220 and one second whipping appts 230 communicated with this second reactor 210.Described second storage tank 220 comprises sulphur storage tank 221, methyl alcohol storage tank 222, sodium methylate storage tank 223 and a dimethylphosphite storage tank 224.Described second whipping appts 230 comprises the second stirring rod 231 extended in the second reactor 210.When reacting, the raw materials such as sulphur storage tank 221, methyl alcohol storage tank 222, sodium methylate storage tank 223 and dimethylphosphite 224 being added the second reactor 210 according to a graded, reacts while stirring.When back has reacted, then add new raw material.
But, when described first reaction member 100 produces described side chain chloro-product, be difficult to accomplish to seal completely, easily occur the situations such as run, drip, leak in process of production.And the gas (as hydrogenchloride) that described side chain chloro-product produces in production process all has stronger toxicity and corrodibility, leak out and easily affect production environment and human body health, be unfavorable for environment protection.Reason has two: the first, because described oxazole [4,5-b] pyridine-2 (3H) ketone is solid feed, when feeding in raw material at every turn, all need hand-fed, and hand-fed must open described first reactor 10, affect the sealing of described first reactor 10.Second, because described first reactor 10 has the first whipping appts 50, the raw material that seal point between first whipping appts 50 and the first reactor 10 easily suffers to produce described side chain chloro-product as sulfur oxychloride and in the reaction the gas that produces as the corrosion of hydrogenchloride, affect the sealing of the first reactor 10, become the hidden danger point can not stopping poisonous gas leakage.
Summary of the invention
In view of this, be necessary to provide a kind of reaction unit for hermetically sealed production methylpyridine phosphorus being beneficial to whole production environment and cleaning, to overcome above-mentioned deficiency.
The invention provides a kind of reaction unit for hermetically sealed production methylpyridine phosphorus, it the 3rd reaction member comprising one first reaction member, one second reaction member and be communicated with respectively with first, second reaction member described.This first reaction member comprises an eddy flow still, an oxazole [4,5-b] pyridine-2 (3H) ketone storage tank, a DMF storage tank, a paraformaldehyde storage tank, monochlor(in)ate sulfoxide storage tank, a gas-holder and a waste gas recovery tank.Described sulfur oxychloride storage tank is communicated with described eddy flow still, and described gas-holder and waste gas recovery tank are all communicated with described eddy flow still.Described first reaction member comprises one first powder liquid mixing pump further, and described first powder liquid mixing pump comprises one first import and one first outlet.Described oxazole [4,5-b] pyridine-2 (3H) ketone storage tank, DMF storage tank and paraformaldehyde storage tank and described first inlet communication, described first outlet is communicated with described eddy flow still.Described eddy flow still comprises a first noumenon and a taper decollator, and described the first noumenon hollow arranges formation one first reaction chamber, and described first reaction chamber is the cone structure of a handstand.The direction that the diameter defining the round tangent plane of described first reaction chamber in axial direction reduces gradually is first direction, and the diameter of the round tangent plane of described taper decollator increases gradually along first direction.
Described eddy flow still comprises one first opening for feed and the first discharge port is separately positioned on the sidewall of described the first noumenon.This first opening for feed is near the larger side of the round tangent plane diameter of described first reaction chamber.This first discharge port is near the less side of the round tangent plane diameter of described first reaction chamber.
Described first opening for feed and described first outlet, described first discharge port all with described 3rd reaction member and the first inlet communication.
Described eddy flow still comprises the passage above the sidewall being arranged on described the first noumenon further, described passage near the larger side of the round tangent plane diameter of the first reaction chamber.
Described eddy flow still also comprises one for inputting the conduit of chlorine, and described taper decollator is a hollow structure, and conduit passes described eddy flow still and is plugged in the taper decollator of described hollow structure.
Described conduit is a Venturi tube.
Described taper decollator is arranged in described the first noumenon, the described axis of taper decollator and the dead in line of the first noumenon.
The internal surface of described the first noumenon and the outside surface interval of described taper decollator are arranged.
Described second reaction member comprises a reactor, a sulphur storage tank, a methyl alcohol storage tank, a sodium methylate storage tank, a dimethylphosphite storage tank and a whipping appts, described methyl alcohol storage tank, sodium methylate storage tank and dimethylphosphite storage tank are communicated with described reactor, and described whipping appts comprises the stirring rod extended in reactor.Described second reaction member comprises one second powder liquid mixing pump further, and described second powder liquid mixing pump comprises one second import and one second outlet, described sulphur storage tank and described second inlet communication, and described second outlet is communicated with described reactor.
Described reactor comprises one second body, described second body hollow arranges formation one second reaction chamber, the shape of described second reaction chamber is tubbiness. described stirring rod extends in described second body, the axis of described stirring rod and the dead in line of the second body, the shape of described second reaction chamber is tubbiness.
Compared to prior art, in the device of production methylpyridine phosphorus provided by the present invention, described first reaction member rear utilizes the inwall along this eddy flow still in pressure directive eddy flow still to flow down by the first powder liquid mixing pump by dispersed for the solid-liquid two-phase raw material in storing pipe.And nationality is by the unique texture of described first reaction chamber and taper decollator, the back cavity progressively narrowed in a space is formed between the first noumenon inwall and taper decollator outer wall, described raw material can not only be made can to rotate at described back cavity fall, and delay the raw material skyborne residence time further by described first reaction chamber and taper decollator.Be appreciated that, by introducing the first powder liquid mixing pump, the eddy flow still with taper first reaction chamber and taper dispersion, one is make the first reaction member without the need to hand-fed, and all reinforced processes all can be carried out in a sealed meter environment; Two is by dispersed for the raw material of solid-liquid two-phase and under making raw material form " whirlwind " helical flow in back cavity by the first powder liquid mixing pump; increase the duration of contact between chlorine and raw material; this effect to stirring of raw material can be made; thus can accomplish in eddy flow still without whipping appts; fundamentally stop poisonous gas leakage, be conducive to environment protection.To sum up; the device of production methylpyridine phosphorus provided by the present invention; because described side chain chloro-product can be produced by the eddy flow still under hermetically sealed environment; therefore, described eddy flow still, when producing described side chain chloro-product, can be accomplished to seal completely; there will not be the situations such as run, drip, leak in process of production; the toxic gas produced also can not leak out, thus it is healthy to affect production environment and human body, is beneficial to cleaning of environment protection and whole production environment.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, embodiments of the invention are described, wherein:
Fig. 1 is the module diagram of traditional device for the production of methylpyridine phosphorus.
Fig. 2 is the structural representation of the first reaction member in Fig. 1.
Fig. 3 is the structural representation of the second reaction member in Fig. 1.
Fig. 4 is the module diagram of a kind of reaction unit for hermetically sealed production methylpyridine phosphorus provided by the invention.
Fig. 5 is the structural representation of the first reaction member in Fig. 4.
Fig. 6 is the structural representation of the second reaction member in Fig. 4.
Embodiment
Based on accompanying drawing, specific embodiments of the invention are further elaborated below.Should be appreciated that specific embodiment described herein is as just embodiment, the protection domain be not intended to limit the present invention.
Referring to Fig. 4, is the module diagram of a kind of reaction unit for hermetically sealed production methylpyridine phosphorus provided by the present invention.Described device comprises first reaction member 400, second reaction member 500, and the 3rd reaction member 600 that first, second reaction member 400,500 described in connects.Described first reaction member 400 is for the production of intermediate product side chain chloro-product.Described second reaction member 500 is for the production of intermediate product thiophosphatephosphorothioate.Above-mentioned two kinds of intermediate products and side chain chloro-product and thiophosphatephosphorothioate finally enter the 3rd reaction member 600, generate the finished product methylpyridine phosphorus after condensation reaction.
Refer to Fig. 5, described first reaction member 400 comprises an eddy flow still 410, multiple the first storage tank, gas-holder 430, waste gas recovery tank 440 and one first powder liquid mixing pump 450 communicated with this eddy flow still 410.
Described first storage tank (figure does not indicate) is for laying in the various raw materials synthesizing described side chain chloro-product.Particularly, described first storage tank comprises an oxazole [4,5-b] pyridine-2 (3H) ketone storage tank 421, DMF (DMF) storage tank 422, paraformaldehyde storage tank 423 and monochlor(in)ate sulfoxide storage tank 424.Wherein, described oxazole [4,5-b] pyridine-2 (3H) ketone storage tank 421, DMF storage tank 422 and paraformaldehyde storage tank 423 are communicated with described eddy flow still 410 by described first powder liquid mixing pump 450.Described sulfur oxychloride storage tank 424 is directly communicated with described eddy flow still 410, to prevent described sulfur oxychloride from directly entering the first powder liquid mixing pump 450 described in the first powder liquid mixing pump 450 and then corrosion damage, also prevent various raw material from reacting in the first powder liquid mixing pump 450 simultaneously.In order to control described oxazole [4,5-b] switch of pyridine-2 (3H) ketone storage tank 421, DMF storage tank 422 and paraformaldehyde storage tank 423 and flow, the connecting pipe of this oxazole [4,5-b] pyridine-2 (3H) ketone storage tank 421, DMF storage tank 422 and paraformaldehyde storage tank 423 and the first powder liquid mixing pump 450 is provided with three control valves (scheming not indicate).Understandably, for controlling switch and the flow of sulfur oxychloride storage tank 424, this sulfur oxychloride storage tank 424 with the connecting pipe of eddy flow still 410 are also provided with a control valve (scheming not indicate).
Described gas-holder 430 stores chlorine, when reacting, by a ventpipe (figure does not indicate), gas is imported eddy flow still 410.For controlling switch and the flow of gas-holder 430, described ventpipe is provided with a control valve (figure does not indicate).440, described waste gas recovery tank reclaims by the recovery tube (figure does not indicate) extend in eddy flow still 410 waste gas reacting and produce.Described waste gas mainly comprises hydrogenchloride.It is emphasized that described waste gas recovery tank 440 means that all can collect the device of described waste gas, as recovery tower.
Described first powder liquid mixing pump 450 has takes out material, feeding, and mixing, the function of dispersed various raw material, for Solid raw materials or solid-liquid mixed-phase feed being carried out dispersed and being sent in eddy flow still 410 and reacting.Particularly, this first powder liquid mixing pump 450 comprises first import 451 and one first outlet 452.Described first import 451 is communicated with described oxazole [4,5-b] pyridine-2 (3H) ketone storage tank 421, DMF storage tank 422 and paraformaldehyde storage tank 423, and described first outlet 452 is communicated with eddy flow still 410.With by raw material (oxazole [4,5-b] pyridine-2 (3H) ketone, DMF and paraformaldehyde) from the first import 451 suck and through mixing, dispersed after, from first outlet 452 with certain pressure, well-mixed material is pressed to eddy flow still 410.Because the raw material of solid-liquid two-phase or solvent also can be carried out mixing press-in eddy flow still 410 automatically by automatic material-absorbing by described first powder liquid mixing pump 450, thus without the need to hand-stuff (as manually added oxazole [4,5-b] pyridine-2 (3H) ketone in solid phase).Namely automatically carry out filler (oxazole [4,5-b] pyridine-2 (3H) ketone in solid phase) by the first powder liquid mixing pump 450, can reaction efficiency be improved, be conducive to the optimization of the healthy of employee and reaction process.
Described eddy flow still 410 comprises a first noumenon 411, a taper decollator 412 be arranged in described the first noumenon 411, first opening for feed 413 being arranged on the sidewall of described the first noumenon 411, one through described taper decollator 412 and for 414, one, conduit inputting chlorine for discharge to produce because producing methylpyridine phosphorus the passage 415 of waste gas (as HCl) and one be arranged on as described in the first discharge port 416 of the first noumenon 411 sidewall.
Described the first noumenon 411 hollow arranges thus is surrounded by its internal surface and forms first reaction chamber, and namely the synthesis of described side chain chloro-product completes in this first reaction chamber.Described first reaction chamber was made up or was formed to described the first noumenon 411 internal surface of acid resisting material is coated with acid resisting material.The shape of described reaction chamber is not limit, and can be barrel-like structure, also can be cone structure.In the present embodiment, described reaction chamber is the cone structure of a handstand, and the direction that the diameter defining the round tangent plane of described first reaction chamber in axial direction reduces gradually is first direction.It is to be noted, this section and even conical structure mentioned in this article, one end that its diameter is less still has one fixed width, namely the diameter of its circle tangent plane is non-vanishing at microcosmic, and just the ratio of the diameter of the round tangent plane of the diameter of the round tangent plane of one end that diameter is less and the larger one end of diameter is less.Therefore from macroscopically, described first reaction chamber is conical structure, and from microcosmic, described first reaction chamber is frustum cone structure.
Described taper decollator 412 is connected with described the first noumenon 411 by one end that circle tangent plane diameter is less, and the internal surface interval of the outside surface of this taper decollator 412 and described the first noumenon 411 is arranged.Wherein, the axis of described taper decollator 412 and the dead in line of the first noumenon 411, and the diameter of the round tangent plane of described taper decollator 412 increases gradually along first direction, make the space between the first reaction chamber and taper decollator 412 outer side wall more and more less along first direction, thus nationality is by the unique texture of described first reaction chamber and taper decollator 412, forms the back cavity progressively narrowed in a space between the first noumenon inwall and taper decollator 412 outer wall.Described raw material can not only be made can to form " whirlwind " rotation at described back cavity fall, delay the raw material skyborne residence time, thus the lowering speed of the contact area be conducive to for increasing powder liquid and reduction powder liquid, improve reaction efficiency.Described taper decollator 412 is a hollow structure, to pass described conduit 414.That is, described chlorine passes through from described taper decollator 412 inside, and other raw materials then pass through from the space between described first reaction chamber and taper decollator 412 outer side wall.Be appreciated that same the first noumenon 411, this taper decollator 412 is also made up of acid resistant material or its Surface coating has acid resistant material.As a same reason, round tangent plane non-vanishing at microcosmic of one end that described taper decollator 412 diameter is less.Therefore from macroscopically, described taper decollator 412 is conical structure, and from microcosmic, described taper decollator 412 is frustum cone structure.
Described first opening for feed 413 is arranged on larger one end of diameter of described first reaction chamber circle tangent plane, flows to the larger one end of taper decollator 412 diameter to make raw material from one end that taper decollator 412 diameter is less.Behind one end less to taper decollator 412 diameter after raw material injects the first reaction chamber from the first opening for feed 413 under stress, major part raw material can rotate around described taper decollator 412 and declines in the space between described the first noumenon 411 internal surface and taper decollator 412 outer side wall, small portion raw material can drop on outside surface or the first noumenon 411 internal surface of taper decollator 412 under gravity, and the outside surface along described the first noumenon 411 internal surface or taper decollator 412 rotates decline.And the internal surface of space between described first reaction chamber and the taper decollator 412 outer side wall outside surface that drops on taper decollator 412 more and more along with highly declining around the raw material that described taper decollator 412 rotates or the first noumenon 411.Because the diameter of taper decollator 412 circle tangent plane increases gradually along first direction, and the diameter of described first reaction chamber circle tangent plane reduces gradually along first direction, this setting can slow down the dropping velocity of the material of outside surface or the first noumenon 411 internal surface dropping on taper decollator 412, can disperse its contact area simultaneously.Meanwhile, because the space between the first reaction chamber and taper decollator 412 outer side wall is more and more less along first direction, when described raw material declines toward first direction, space is more crowded, thus can slow down the dropping velocity of described material further.Be appreciated that described raw material is longer in the residence time in space, the contact area between each raw material is larger, and contact more abundant, reaction efficiency is higher.
Described conduit 414 can be a Venturi tube, its hermetically passing the first noumenon 411, and be plugged in the taper decollator 412 of hollow structure, thus fix the position of this conduit 414, the chlorine entered from conduit 414 can also be made to rising simultaneously, and then fully contact with defluent raw material, reach the object of fully reaction further.Be appreciated that, evenly flowing out from described taper decollator 412 for enabling described chlorine and increase the contact area of being detained skyborne raw material with the first reaction chamber, the sidewall of described taper decollator 412 also evenly can be provided with multiple through hole (scheming not indicate).Further, when the larger one end of described taper decollator 412 diameter is covered by reaction solution (solution after raw material and chlorine reaction), by described through hole, described chlorine can directly and contact raw.
Described passage 415 is also salable to be arranged on the first noumenon 411, and when chlorine and the oxazole pyridone taking DMF as dissolution with solvents, paraformaldehyde, when the raw material reactions such as sulfur oxychloride generate waste gas (as HCl), described waste gas can be discharged from this passage 415.
Described first discharge port 416 is communicated with described first powder liquid mixing pump 450 and the 3rd reaction member 600 simultaneously.For controlling, from described eddy flow still 410 raw material out or product stream to the first powder liquid mixing pump 450 and the 3rd reaction member 600, to be provided with control valve (scheming not indicate) between the first import 451 of described first powder liquid mixing pump 450 and described first discharge port 416.Because first entrance 451 of described first discharge port 416 with described first powder liquid mixing pump 450 is communicated with.When reaction does not complete, unreacted completely raw material can carry out blending dispersion again by being sent to described first powder liquid mixing pump 450, directive eddy flow still 410 again after being uniformly dispersed, thus raising reaction efficiency, avoid deposits materials to contact bottom described eddy flow still 410 not exclusively, cause reaction not exclusively.When the reactions are completed, described reacted product can flow to the 3rd reaction member 600, carries out next step reaction.
Refer to Fig. 6, described second reaction member 500 comprises a reactor 510, multiple the second storage tank (scheming not indicate), one second powder liquid mixing pump 530 and whipping appts 540 communicated with this reactor 510.
Described second storage tank is for laying in the various raw materials of the described thiophosphatephosphorothioate of synthesis.Particularly, described second storage tank comprises sulphur storage tank 521, methyl alcohol storage tank 522, sodium methylate storage tank 523 and a dimethylphosphite storage tank 524.Described sulphur storage tank 521 is communicated with described reactor 510 by described second powder liquid mixing pump 530.Described methyl alcohol storage tank 522, sodium methylate storage tank 523 and dimethylphosphite storage tank 524 is directly communicated with described reactor 510, directly enter the second powder liquid mixing pump 530 to avoid described raw material and then corrode described second powder liquid mixing pump 530, described raw material also can be avoided simultaneously to react in the second powder liquid mixing pump 530.In order to control switch and the flow of described sulphur storage tank 521, the connecting pipe of this sulphur storage tank 521 and the second powder liquid mixing pump 530 is respectively arranged with control valve (scheming not indicate).Understandably, for controlling switch and the flow of described methyl alcohol storage tank 522, sodium methylate storage tank 523 and dimethylphosphite storage tank 524, this methyl alcohol storage tank 522, sodium methylate storage tank 523 and dimethylphosphite storage tank 524 with the connecting pipe of reactor 510 are also provided with a control valve (scheming not indicate) separately.
Described second powder liquid mixing pump 530 has takes out material, feeding, and the function of blending dispersion, for by dispersed for Solid raw materials (as sulphur) and be sent to reactor 510.Particularly, this second powder liquid mixing pump 530 comprises second import 531 and one second outlet 532.Described second import 531 is communicated with described sulphur storage tank 521, and described second outlet 532 is communicated with reactor 510.Raw material (as sulphur) is sucked from the second import 531 and after dispersed, with certain pressure, the material fully disperseed is pressed to reactor 510 from the second outlet 532.Because Solid raw materials also can be carried out mixing press-in reactor 510 automatically by automatic material-absorbing by described second powder liquid mixing pump 530, thus without the need to hand-stuff (as manually added the sulphur in solid phase).Namely automatically carry out filler by the second powder liquid mixing pump 530, can reaction efficiency be improved, be conducive to the optimization of the healthy of employee and reaction process.
Described reactor 510 comprises the second opening for feed 512 and second discharge port 513 be arranged on bottom described second body 511 that second body 511, is arranged on the sidewall of described second body 511.
Described second body 511 hollow arranges thus forms second reaction chamber, and namely the synthesis of described thiophosphatephosphorothioate completes in this second reaction chamber.Described second reaction chamber was made up or was formed to described second body 511 internal surface of acid resisting material is coated with acid resisting material.The shape of described second reaction chamber is not limit, and can be barrel-like structure, also can be cone structure.In the present embodiment, described second reaction chamber is the barrel-like structure of a handstand.
The axis of described second opening for feed 512 and the axis at intervals of described second discharge port 513 are arranged, and preferably, the axis of described second opening for feed 512 is mutually vertical with the axis of described second discharge port 513.Described second opening for feed 512 exports 532 with second of described second powder liquid mixing pump 530 and is communicated with.
Described second discharge port 513 is communicated with described second powder liquid mixing pump 530 and the 3rd reaction member 600 simultaneously.For controlling from described reactor 510 raw material out or product stream to the second powder liquid mixing pump 530 and the 3rd reaction member 600, be provided with a control valve (scheming not indicate) between second import 531 of described second powder liquid mixing pump 530 and described second discharge port 513, between described second discharge port 513 and the 3rd reaction member 600, be also provided with a control valve (scheming not indicate).When reaction does not complete, unreacted completely raw material can carry out blending dispersion again by the second powder liquid mixing pump 530, directive reactor 510 again after being uniformly dispersed, thus raising reaction efficiency, avoid deposits materials to contact bottom described reactor 510 not exclusively, cause reaction not exclusively.When the reactions are completed, described reacted product can flow to the 3rd reaction member 600, carries out next step reaction.
Described whipping appts 540 is for stirring raw material when reacting, fully to disperse the raw material in reactor 510.This whipping appts 540 comprises the stirring rod 541 extended in described second body 511, the axis of described stirring rod 541 and the dead in line of the second body 511, to reach best mixing effect.
Compared to prior art, in the device of production methylpyridine phosphorus provided by the present invention, described first reaction member rear utilizes the inwall along this eddy flow still in pressure directive eddy flow still to flow down by the first powder liquid mixing pump by dispersed for the solid-liquid two-phase raw material in storing pipe.And nationality is by the unique texture of described first reaction chamber and taper decollator, the back cavity progressively narrowed in a space is formed between the first noumenon inwall and taper decollator outer wall, described raw material can not only be made can to rotate at described back cavity fall, and delay the raw material skyborne residence time further by described first reaction chamber and taper decollator.Be appreciated that, by introducing the first powder liquid mixing pump, the eddy flow still with taper first reaction chamber and taper dispersion, one is make the first reaction member without the need to hand-fed, and all reinforced processes all can be carried out in a sealed meter environment; Two is by dispersed for the raw material of solid-liquid two-phase and under making raw material form " whirlwind " helical flow in back cavity by the first powder liquid mixing pump; increase the duration of contact between chlorine and raw material; raw material can be made to reach the effect of stirring; thus can accomplish in eddy flow still without whipping appts; fundamentally stop poisonous gas leakage, be conducive to environment protection.To sum up; the device of production methylpyridine phosphorus provided by the present invention; because described side chain chloro-product can be produced by the eddy flow still under hermetically sealed environment; therefore, described eddy flow still, when producing described side chain chloro-product, can be accomplished to seal completely; there will not be the situations such as run, drip, leak in process of production; the toxic gas produced also can not leak out, thus it is healthy to affect production environment and human body, is beneficial to cleaning of environment protection and whole production environment.
Be appreciated that, the reaction unit for hermetically sealed production methylpyridine phosphorus in the application is not only applicable to for the production of methylpyridine phosphorus, also can be applicable to major part produce in the chemical reaction of waste gas, be especially applicable to produce in other reaction process and produce with obnoxious flavour and need to use the chemical substance of mechanical stirring device equipment.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all do in the spirit and principles in the present invention any amendment, equivalent to replace and improvement etc., all should be included in protection scope of the present invention.
Claims (10)
1. the reaction unit for hermetically sealed production methylpyridine phosphorus, it comprises one first reaction member, one second reaction member and with described first, the 3rd reaction member that second reaction member is communicated with respectively, this first reaction member comprises an eddy flow still, one oxazole [4, 5-b] pyridine-2 (3H) ketone storage tank, one N, dinethylformamide storage tank, one paraformaldehyde storage tank, monochlor(in)ate sulfoxide storage tank, one gas-holder and a waste gas recovery tank, described sulfur oxychloride storage tank is communicated with described eddy flow still, described gas-holder and waste gas recovery tank are all communicated with described eddy flow still, it is characterized in that: described first reaction member comprises one first powder liquid mixing pump further, described first powder liquid mixing pump comprises one first import and one first outlet, described oxazole [4,5-b] pyridine-2 (3H) ketone storage tank, N, dinethylformamide storage tank and paraformaldehyde storage tank and described first inlet communication, described first outlet is communicated with described eddy flow still, described eddy flow still comprises the taper decollator that the first noumenon described in a first noumenon and connects, described the first noumenon hollow arranges formation one first reaction chamber, described first reaction chamber is the conical structure of a handstand, and described sulfur oxychloride storage tank is arranged on the larger side of the round tangent plane diameter of described first reaction chamber, the direction that the diameter defining the round tangent plane of described first reaction chamber in axial direction reduces gradually is first direction, and the diameter of the round tangent plane of described taper decollator increases gradually along first direction.
2., as claimed in claim 1 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described eddy flow still comprises one first opening for feed and the first discharge port is separately positioned on the sidewall of described the first noumenon; This first opening for feed is near the larger side of the round tangent plane diameter of described first reaction chamber; This first discharge port is near the less side of the round tangent plane diameter of described first reaction chamber.
3., as claimed in claim 2 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described first opening for feed and described first outlet, described first discharge port all with described 3rd reaction member and the first inlet communication.
4. as claimed in claim 2 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described eddy flow still comprises the passage above the sidewall being arranged on described the first noumenon further, described passage near the larger side of the round tangent plane diameter of the first reaction chamber and being communicated with waste gas recovery tank.
5. as claimed in claim 1 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described eddy flow still also comprises one for inputting the conduit of chlorine, described taper decollator is a hollow structure, and conduit passes described eddy flow still and is plugged in the taper decollator of described hollow structure.
6., as claimed in claim 5 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described conduit is a Venturi tube.
7., as claimed in claim 1 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described taper decollator is arranged in described the first noumenon, the described axis of taper decollator and the dead in line of the first noumenon.
8. as claimed in claim 1 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: the internal surface of described the first noumenon and the outside surface interval of described taper decollator are arranged, and form a back cavity between described the first noumenon and taper decollator.
9. as claimed in claim 1 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described second reaction member comprises a reactor, a sulphur storage tank, a methyl alcohol storage tank, a sodium methylate storage tank, a dimethylphosphite storage tank and a whipping appts, described methyl alcohol storage tank, sodium methylate storage tank and dimethylphosphite storage tank are communicated with described reactor, and described whipping appts comprises the stirring rod extended in reactor; Described second reaction member comprises one second powder liquid mixing pump further, and described second powder liquid mixing pump comprises one second import and one second outlet, described sulphur storage tank and described second inlet communication, and described second outlet is communicated with described reactor.
10., as claimed in claim 9 for the reaction unit of hermetically sealed production methylpyridine phosphorus, it is characterized in that: described reactor comprises one second body, described second body hollow arranges formation one second reaction chamber, and the shape of described second reaction chamber is tubbiness; Described stirring rod extends in described second body, the axis of described stirring rod and the dead in line of the second body, and the shape of described second reaction chamber is tubbiness.
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| CN101234308A (en) * | 2008-03-05 | 2008-08-06 | 聂如国 | Powder-liquid mixer |
| CN201664601U (en) * | 2010-04-22 | 2010-12-08 | 海门贝斯特精细化工有限公司 | Vacuum automatic feeding device |
| CN102329253A (en) * | 2011-03-22 | 2012-01-25 | 江苏中丹集团股份有限公司 | Reaction apparatus for resorcinol neutralization reaction section and reaction technology thereof |
| CN202989028U (en) * | 2012-12-19 | 2013-06-12 | 宁波远利化工有限公司 | Reaction device used for full-sealed production of azamethiphos |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101234308A (en) * | 2008-03-05 | 2008-08-06 | 聂如国 | Powder-liquid mixer |
| CN201664601U (en) * | 2010-04-22 | 2010-12-08 | 海门贝斯特精细化工有限公司 | Vacuum automatic feeding device |
| CN102329253A (en) * | 2011-03-22 | 2012-01-25 | 江苏中丹集团股份有限公司 | Reaction apparatus for resorcinol neutralization reaction section and reaction technology thereof |
| CN202989028U (en) * | 2012-12-19 | 2013-06-12 | 宁波远利化工有限公司 | Reaction device used for full-sealed production of azamethiphos |
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