CN106008598A - Preparation method of 1, 6-dihexyl triamine pentamethylenophosphonic acid - Google Patents

Preparation method of 1, 6-dihexyl triamine pentamethylenophosphonic acid Download PDF

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Publication number
CN106008598A
CN106008598A CN201610378182.5A CN201610378182A CN106008598A CN 106008598 A CN106008598 A CN 106008598A CN 201610378182 A CN201610378182 A CN 201610378182A CN 106008598 A CN106008598 A CN 106008598A
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Prior art keywords
reactor
formaldehyde
preparation
salt
reaction
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CN201610378182.5A
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Chinese (zh)
Inventor
顾仁杰
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Changzhou Yao's Tongde Chemical Co Ltd
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Changzhou Yao's Tongde Chemical Co Ltd
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Priority to CN201610378182.5A priority Critical patent/CN106008598A/en
Publication of CN106008598A publication Critical patent/CN106008598A/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • C07F9/3804Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)] not used, see subgroups
    • C07F9/3808Acyclic saturated acids which can have further substituents on alkyl
    • C07F9/3817Acids containing the structure (RX)2P(=X)-alk-N...P (X = O, S, Se)

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)

Abstract

The invention relates to the technical field of chemical industry, in particular to a preparation method of dihexyl triamine pentamethylenophosphonic acid. The method comprises the steps of: (1) adding bishexamethylenetriamine and water into a reaction kettle, performing cooling to less than 25DEG, starting adding 31% hydrochloric acid dropwise to carry out salt-forming reaction for 2h; (2) adding phosphorous acid into the reaction kettle, performing heating to 80-110DEG C, and carrying out reaction for 3-8h; and (3) transferring all the materials into an elevated tank, adjusting the temperature of the reaction kettle to 120-150DEG C, adding the materials in the elevated tank dropwise into the reaction kettle slowly, and keeping the temperature in the reaction kettle at 120-150DEG C, and performing heat preservation for 2-3h at the end of dropwise adding. The method provided by the invention avoids the material-spraying phenomenon in the final distillation process, also can reduce the residual formaldehyde of the final product from 2-3% to 10mg/L, and the chloride from original 6-8% to 100mg/L.

Description

A kind of preparation method of 1,6-dihexyl triamine pentamethylene phosphonic acids
Technical field
The present invention relates to chemical technology field, particularly relate to a kind of 1, the preparation of 6-dihexyl triamine pentamethylene phosphonic acids Method.
Background technology
1,6-dihexyl triamine pentamethylene phosphonic acids, in addition to using as corrosion inhibiting and descaling agent at water treatment field, it is possible to To use as chelating agen, hydrogen peroxide bleaching stabilizer in electronics, printing and dyeing assistant field.But 1,6-dihexyl triamine pentamethylene phosphonic acids Use as printing and dyeing assistant and there is substantial amounts of residues of formaldehyde, dyeing has clear and definite limit for harmful substances such as removing residue formaldehydes System.
Prior art is so process for problem above: owing to 1,6-dihexyl triamine pentamethylene phosphonic acids is one Plant macromolecule organophosphor, and two hexene triamines in production process are the co-product producing essence hexamethylene diamine, in process of production, should After target product generates, the formaldehyde of excess and hydrogen chloride use the method for distillation to remove, due to by dihexyl triamine purity and product The factor impact that product molecular weight is high, 1, controls temperature still-process after the reaction completely of 6-dihexyl triamine pentamethylene phosphonic acids In, often material can occur material spray phenomenon.
Summary of the invention
The present invention is in order to overcome the deficiency of above-mentioned technical problem, it is provided that a kind of 1,6-dihexyl triamine pentamethylene phosphonic acids Preparation method, the method can be fully solved above-mentioned technical problem.
The technical scheme solving above-mentioned technical problem is as follows:
A kind of 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, comprise the following steps:
(1) salt is become: two hexene triamines and water are put in reactor, be cooled to less than the 25 DEG C hydrochloric acid starting to drip 31% Carry out salt-forming reaction 2 hours, during salt-forming reaction, have hydrogen chloride to produce;
(2) condensation: phosphorous acid is put in reactor after terminating by salt-forming reaction, is heated to 80~110 DEG C, is dripped by a high position Add groove dropping formaldehyde, drip insulation backflow 3~8 hours, hydrogen chloride, formaldehyde exhaust-gas and the steam produced in course of reaction After condensed in two stages, formalin reclaims, and does not coagulates gas and enters device for absorbing tail gas, and the described gas bag that do not coagulates includes hydrogen chloride, water Steam and a small amount of formaldehyde;
(3) refined: the material in reactor is fully transferred in head tank, then the temperature of reactor is adjusted to 120~150 DEG C, then material in head tank is slowly added dropwise to reactor, and to keep the temperature of reactor be 120~150 DEG C, drip complete insulation 2~3 hours.
Two hexene triamines, water, phosphorous acid, the mass ratio of formaldehyde are 1:5:3:3.
Rate of addition described in step (3) is 800~1000kg/h.
Reaction equation is as follows:
The present invention provides a kind of 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, it is to avoid last still-process The phenomenon of middle material spray, and end product removing residue formaldehyde can be reduced to 10mg/L by 2~3%, chloride by original 6~ 8% is reduced to 100mg/L.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the present invention is further detailed explanation.
Embodiment 1:
A kind of 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, comprise the following steps:
(1) salt is become: two hexene triamines and water are put in reactor, be cooled to less than the 25 DEG C hydrochloric acid starting to drip 31% Carry out salt-forming reaction 2 hours, during salt-forming reaction, have hydrogen chloride to produce;
(2) condensation: phosphorous acid is put in reactor after terminating by salt-forming reaction, is heated to 80 DEG C, by high-order dropwise adding tank Dropping formaldehyde, drips insulation backflow 8 hours, and the hydrogen chloride, formaldehyde exhaust-gas and the steam that produce in course of reaction are through two-stage After condensation, formalin reclaims, and does not coagulates gas and enters device for absorbing tail gas, described do not coagulate gas bag include hydrogen chloride, steam and A small amount of formaldehyde;
It is (3) refined: the material in reactor to be fully transferred in head tank, the temperature of reactor is adjusted to 150 DEG C, Then material in head tank is slowly added dropwise to reactor, and to keep the temperature of reactor be 150 DEG C, drip complete insulation 2 Hour.
Two hexene triamines, water, phosphorous acid, the mass ratio of formaldehyde are 1:5:3:3.
Rate of addition described in step (3) is 800kg/h.
Embodiment 2:
A kind of 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, comprise the following steps:
(1) salt is become: two hexene triamines and water are put in reactor, be cooled to less than the 25 DEG C hydrochloric acid starting to drip 31% Carry out salt-forming reaction 2 hours, during salt-forming reaction, have hydrogen chloride to produce;
(2) condensation: phosphorous acid is put in reactor after terminating by salt-forming reaction, is heated to 110 DEG C, by high-order dropwise adding tank Dropping formaldehyde, drips insulation backflow 3 hours, and the hydrogen chloride, formaldehyde exhaust-gas and the steam that produce in course of reaction are through two-stage After condensation, formalin reclaims, and does not coagulates gas and enters device for absorbing tail gas, described do not coagulate gas bag include hydrogen chloride, steam and A small amount of formaldehyde;
It is (3) refined: the material in reactor to be fully transferred in head tank, the temperature of reactor is adjusted to 120 DEG C, Then material in head tank is slowly added dropwise to reactor, and to keep the temperature of reactor be 120 DEG C, drip complete insulation 3 Hour.
Two hexene triamines, water, phosphorous acid, the mass ratio of formaldehyde are 1:5:3:3.
Rate of addition described in step (3) is 1000kg/h.
Embodiment 3:
A kind of 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, comprise the following steps:
(1) salt is become: two hexene triamines and water are put in reactor, be cooled to less than the 25 DEG C hydrochloric acid starting to drip 31% Carry out salt-forming reaction 2 hours, during salt-forming reaction, have hydrogen chloride to produce;
(2) condensation: phosphorous acid is put in reactor after terminating by salt-forming reaction, is heated to 100 DEG C, by high-order dropwise adding tank Dropping formaldehyde, drips insulation backflow 5 hours, and the hydrogen chloride, formaldehyde exhaust-gas and the steam that produce in course of reaction are through two-stage After condensation, formalin reclaims, and does not coagulates gas and enters device for absorbing tail gas, described do not coagulate gas bag include hydrogen chloride, steam and A small amount of formaldehyde;
It is (3) refined: the material in reactor to be fully transferred in head tank, the temperature of reactor is adjusted to 140 DEG C, Then material in head tank is slowly added dropwise to reactor, and to keep the temperature of reactor be 140 DEG C, drip complete insulation 2.5 hour.
Two hexene triamines, water, phosphorous acid, the mass ratio of formaldehyde are 1:5:3:3.
Rate of addition described in step (3) is 900kg/h.
The present invention provides a kind of 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, it is to avoid last still-process The phenomenon of middle material spray, and end product removing residue formaldehyde can be reduced to 10mg/L by 2~3%, chloride by original 6~ 8% is reduced to 100mg/L.
The above, be only presently preferred embodiments of the present invention, and the present invention not does any pro forma restriction, every depends on According to any simple modification in the technical spirit of the present invention, above example made, equivalent variations, each fall within the guarantor of the present invention Within the scope of protecting.

Claims (3)

1. one kind 1, the preparation method of 6-dihexyl triamine pentamethylene phosphonic acids, it is characterised in that comprise the following steps:
(1) salt is become: two hexene triamines and water are put in reactor, be cooled to less than the 25 DEG C hydrochloric acid starting to drip 31% and carry out Salt-forming reaction 2 hours, has hydrogen chloride to produce during salt-forming reaction;
(2) condensation: phosphorous acid is put in reactor after terminating by salt-forming reaction, is heated to 80~110 DEG C, by high-order dropwise adding tank Dropping formaldehyde, drips insulation backflow 3~8 hours, and the hydrogen chloride, formaldehyde exhaust-gas and the steam that produce in course of reaction are through two After level condensation, formalin reclaims, and does not coagulates gas and enters device for absorbing tail gas, and the described gas bag that do not coagulates includes hydrogen chloride, steam With a small amount of formaldehyde;
(3) refined: the material in reactor to be fully transferred in head tank, the temperature of reactor is adjusted to 120~150 DEG C, then material in head tank is slowly added dropwise to reactor, and to keep the temperature of reactor be 120~150 DEG C, drip Bi Baowen 2~3 hours.
The preparation method of the most according to claim 1 a kind of 1,6-dihexyl triamine pentamethylene phosphonic acids, it is characterised in that Two hexene triamines, water, phosphorous acid, the mass ratio of formaldehyde are 1:5:3:3.
The preparation method of the most according to claim 1 a kind of 1,6-dihexyl triamine pentamethylene phosphonic acids, it is characterised in that Rate of addition described in step (3) is 800~1000kg/h.
CN201610378182.5A 2016-05-31 2016-05-31 Preparation method of 1, 6-dihexyl triamine pentamethylenophosphonic acid Pending CN106008598A (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101323627A (en) * 2008-07-07 2008-12-17 河南清水源科技股份有限公司 Bis(hexamethylene triamine penta (methylene phosphonic acid)) and production process thereof
CN104844649A (en) * 2015-05-26 2015-08-19 周峰 Preparation method of bis(hexamethylene triamine penta (methylene phosphonic acid))

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101323627A (en) * 2008-07-07 2008-12-17 河南清水源科技股份有限公司 Bis(hexamethylene triamine penta (methylene phosphonic acid)) and production process thereof
CN104844649A (en) * 2015-05-26 2015-08-19 周峰 Preparation method of bis(hexamethylene triamine penta (methylene phosphonic acid))

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
化学工业部科学技术情报研究所: "《化工产品手册 有机化工原料 上册》", 28 February 1985, 化学工业出版社 *
李彬 等: "新型亚甲基膦酸水处理剂的合成及阻垢性能研究", 《工业水处理》 *

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Application publication date: 20161012