CN103864982B - Preparation method of fluorinated acrylate emulsion - Google Patents

Preparation method of fluorinated acrylate emulsion Download PDF

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CN103864982B
CN103864982B CN201310695104.4A CN201310695104A CN103864982B CN 103864982 B CN103864982 B CN 103864982B CN 201310695104 A CN201310695104 A CN 201310695104A CN 103864982 B CN103864982 B CN 103864982B
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emulsion
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acrylate
monomer
methacrylate
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CN103864982A (en
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李义涛
郑炳发
汤诚
杨策宇
王寅飞
邹智杰
游孟梦
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Ruyuan Yao Autonomous County Dongyangguang Formed Foil Co Ltd
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Dongguan Dongyang Guangke Research and Development Co Ltd
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Abstract

The invention relates to a preparation method of a fluorinated acrylate emulsion. A method of semi-continuous seed emulsion polymerization is used, so that a fluorine monomer is concentrated in a copolymer shell; meanwhile, a reactive emulsifier is used, so that emulsifier molecules are combined on the surface of emulsion particles via stable covalent bonds. Specific method comprises the following steps: firstly, preparing a nuclear emulsion, dropping a shell preemulsion on the basis of the shell preemulsion, and polymerizing through a semi-continuous seed method to obtain an aqueous fluorinated acrylate shell emulsion. Due to the preparation technique, a fluorine-containing monomer is placed in the shell, so that the efficiency is maximized, advantages of a fluorine-containing polymer is shown as much as possible; the emulsion obtained through the method has excellent storage stability, calcium ion stability, freeze-thaw stability and mechanical stability.

Description

A kind of preparation method of fluorinated acrylate emulsion
Technical field
The present invention relates to coating emulsion and production technical field, and in particular to a kind of preparation of fluorinated acrylate emulsion Method.
Background technology
Aqueouss (methyl) series of acrylate coating has good good film-forming property, application property, film alkali resistance and colour retention Good, pollution-free the advantages of, it is widely applied.But (methyl) emulsion acrylic resin heat-resisting quantity is poor, in building coating Most significantly have the disadvantage that high temperature after-tacks, and causes stain resistance to decline using in, resistance to water and weather resisteant are poor, so which uses model Enclose and be restricted.In order to obtain the coating of excellent performance, people are grafted a number of fluorochemical monomer in acrylic resin and enter Row is modified, can keep the original advantage of acrylate copolymer, gives its excellent weatherability, resistance to water, oil resistivity, resistance to again The features such as hot and stain resistance, so as to be with a wide range of applications, but the price of fluorinated acrylate monomer is very high, Excessive use such monomer, will certainly improve the price of modified acrylate polymer.
Therefore, on the premise of fluoropolymer plurality of advantages is maximized, how to reduce fluorinated acrylate emulsion cost Become focus of concern.Simultaneously because the conventional emulsion agent molecule used in emulsion polymerization is easily affected by external environment Generation is parsed, and makes emulsion particle collide cohesion, and after emulsion film forming, remains emulsifier molecules in the polymer, easily poly- There is migration in compound and cause the resistance to water of polymeric film to decline.
The content of the invention
It is an object of the invention to provide a kind of preparation method of the fluorinated acrylate emulsion with nucleocapsid structure, is reducing During the consumption of fluorine monomer, make emulsion that still there is excellent weatherability, resistance to soiling, resistance to water and resistance to acids and bases.Simultaneously using anti- Type emulsifying agent is answered, and emulsifier molecules is made with more stable covalent with reference on emulsion particle surface, so that the emulsion tool for obtaining There are excellent bin stability, Calcium ion stability, freeze-thaw stability and mechanical stability.
Hud typed fluorine-containing (methyl) acrylic acid ester emulsion of the present invention is by monomer, the moon/non-emulsifierses, response type emulsifying Agent, water, initiator and pH adjusting agent, are obtained using the polymerization of semi-continuous seed method Jing after pre-emulsification.Seed emulsion is prepared first, Then shell pre-emulsion is will be enriched in after the shell monomer mixture pre-emulsification of fluorine monomer obtaining, using the method for Deca by shell pre-emulsion Deca Target product is obtained after reacting in seed emulsion.
The purpose of the present invention is achieved through the following technical solutions:
One technical scheme of the present invention provides a kind of preparation method of fluorinated acrylate emulsion, comprising following step Suddenly:
1)Prepare pre-emulsion
I)The preparation of core pre-emulsion
After by anion emulsifier, nonionic emulsifier, reactive emulsifier, initiator and deionized water stirring and dissolving, The methacrylate-based monomer and acrylic ester monomer mixed liquor with or without fluoroalkyl class monomer is added, is stirred Mix pre-emulsification and prepare core pre-emulsion, wherein each component mass parts are:
II)The preparation of shell pre-emulsion
After anion emulsifier, nonionic emulsifier, initiator and deionized water stirring and dissolving, add containing fluoroalkyl third Olefin(e) acid esters monomer and the mixed solution of functional monomer, stir pre-emulsification and prepare shell pre-emulsion, and wherein each component mass parts are:
2)The preparation of seed emulsion
Take step 1)The 20-50% of obtained core pre-emulsion, stirs under inert gas shielding, is warming up to 70-90 DEG C, treats temperature After degree is stable, residual nucleus emulsion is dripped, afterwards insulation reaction, seed emulsion is obtained;
3)Prepare fluorinated acrylate emulsion
It is kept stirring for, inert gas shielding, temperature are maintained under the conditions of 70-90 DEG C, to step 2)Gained seed emulsion drop Add step 1)Obtained shell pre-emulsion, drop finish insulation reaction, after reaction completely, are down to 10-30 DEG C, Deca pH adjusting agent to pH It is worth for 7.0-8.5, mixed liquor filters to obtain fluorinated acrylate emulsion.
According to the preparation method that above-mentioned technical proposal is provided, in some embodiments, the acrylic ester monomer choosing From acrylic acid methyl ester., ethyl acrylate, butyl acrylate, Isooctyl acrylate monomer, lauryl acid esters, Process Conditions of Cetane Acrylate or Octadecyl acrylate.
According to the preparation method that above-mentioned technical proposal is provided, in some embodiments, the methyl acrylic ester list Body is selected from methyl methacrylate, ethyl methacrylate, butyl methacrylate, methacrylic acid cyclohexanol, metering system Sour lauryl or octadecyl methacrylate.
It is according to the preparation method that above-mentioned technical proposal is provided, in some embodiments, described containing fluoroalkyl Class monomer is compound shown in Formulas I
Wherein R1Selected from H or methyl, R2Selected from C2-C20Containing fluoroalkyl.
In some embodiments, the fluorine-containing alkylacrylate monomer selected from trifluoroethyl methacrylate, third Olefin(e) acid hexafluoro butyl ester, perluorooctyl acrylate, dodecafluoroheptyl methacrylate, perfluoro butyl ethyl propylene acid esters, perfluor Butyl ethyl methacrylate, perfluoro hexyl ethylmethyl acrylate, perfluorooctylethyl group acrylate or perfluoro capryl Ethylmethyl acrylate.
According to the preparation method that above-mentioned technical proposal is provided, in some embodiments, the functional monomer is selected from first Base acrylic acid, hydroxyethyl methylacrylate, Hydroxypropyl methacrylate, methacrylonitrile, acrylic acid, 2-(Acryloyloxy)ethanol, third Olefin(e) acid hydroxypropyl acrylate, acrylonitrile, acrylamide, N hydroxymethyl acrylamide, Ethylene glycol dimethacrylate, diacetone acrylamide acyl Amine or adipic acid dihydrazide.
According to the preparation method that above-mentioned technical proposal is provided, in some embodiments, the reactive emulsifier is selected from 2- propenyl ether -3- hydroxy propane -1- sodium sulfonates, alkyl phenol allyl polyether sulfate, 2- acrylamide -2- methylpropane sulphurs Acid sodium-salt, allyloxy NPE ammonium sulfate, sodium vinyl sulfonate, allyl polyether sulfate or allyloxy Fatty alcohol oxygen ethylene ether ammonium sulfate.
According to the preparation method that above-mentioned technical proposal is provided, in some embodiments, the anion emulsifier is selected from Sodium lauryl sulphate, dodecylbenzene sodium sulfonate, 1,2- dodecyl diether disulfonates, decyl polyoxyethylene ether succinum Acid monoester disodium sulfonate salt, NPE ammonium sulfate, NPE monomester succinate disodium sulfonate salt Or polyoxyethylenated alcohol sodium sulfate.
This preparation method provided according to above-mentioned technical proposal, in some embodiments, the nonionic emulsifier is Fatty alcohol-polyoxyethylene ether, OPEO or NPE.
According to the preparation method that above-mentioned technical proposal is provided, in some embodiments, the initiator is persulfate.
In some embodiments, persulfate is selected from sodium peroxydisulfate, potassium peroxydisulfate or Ammonium persulfate..
According to above-mentioned technical proposal provide preparation method, in some embodiments, the pH adjusting agent selected from ammonia, Alkali-metal carbonate, bicarbonate, phosphate or hydrophosphate.
In other embodiments, pH adjusting agent of the present invention is selected from ammonia, sodium carbonate, sodium bicarbonate, phosphoric acid hydrogen Disodium, potassium carbonate, potassium hydrogen phosphate or dipotassium hydrogen phosphate or its combination.
Another technical scheme of the present invention provides the fluorine-containing propene prepared using the method that above-mentioned technical proposal is provided Acid esters emulsion is for the application in building coating is prepared.
Unless explicitly stated otherwise in contrast, otherwise, all scopes that the present invention is quoted include end value.For example, it is coated on After base material, " being warming up to 70-90 DEG C " represents that temperature range T for heating up is 70 DEG C≤T≤90 DEG C.
The end value that the present invention is quoted potentially includes 0, when a certain end value is 0, represents that its content for representing is optional, example Such as, in ingredient lists, " fluorine-containing alkylacrylate monomer 0-6.0 parts " is represented in some embodiments it is possible to without containing Fluoroalkyl class monomer.
Terminology used in the present invention "or" represents alternative, if appropriate, can combine them, that is, Say, term "or" includes independent alternative and combinations thereof listed by each.For example, " pH adjusting agent selected from ammonia, Alkali-metal carbonate, bicarbonate, phosphate or hydrophosphate " represents that pH adjusting agent can be ammonia, alkali-metal carbonic acid Salt, bicarbonate, phosphate, one kind of hydrophosphate, or its more than one combination.
The beneficial effects of the present invention is:The present invention is using (methyl) acrylic ester monomer and contains fluoroalkyl Method of the class monomer by semi-continuous seed emulsion polymerization, prepares the fluorinated acrylate emulsion with nucleocapsid structure, acquisition Emulsion is on the basis of (methyl) acrylic acid ester emulsion excellent properties are maintained, and the characteristic with fluorine, and due to fluorine-containing list Body is enriched on the surface of copolymer, when the consumption of fluorine monomer is reduced, still fully demonstrates the excellent chemically-resistants of C-F Property, uvioresistant and antioxygenic property.Whole course of reaction adopts Deca mode, and the fluorinated acrylate emulsion solid content of acquisition is big In 40%, while latex particle size is less in emulsion, particle diameter distribution is narrower, with excellent bin stability, dilution stability, Freeze-thaw stability and mechanical stability, and preparation process is simple, easy control of reaction conditions can be widely applied to building, industry The fields such as coating, textile finishing and leather finish.
Specific embodiment
Described below is the preferred embodiment of the present invention, and what the present invention was protected is not limited to the following side of being preferable to carry out Formula.It should be pointed out that for a person skilled in the art on the basis of this innovation and creation design, some deformations for making and Improve, belong to protection scope of the present invention.
Embodiment 1
By deionized water 125.0g, sodium lauryl sulphate 1.0g, OPEO 2.0g, 2- propenyl ether- After 3- hydroxy propane -1- sodium sulfonate 1.5g, potassium peroxydisulfate 0.5g stirring and dissolving, be slowly added to methyl methacrylate 58.0g with The mixed liquor of butyl acrylate 58.0g, high speed machine stirring pre-emulsification 45 minutes, obtains 246.0g pre-emulsion I;
By deionized water 53.0g, sodium lauryl sulphate 0.4g, OPEO 0.8g, potassium peroxydisulfate 0.25g After stirring and dissolving, the mixed liquor of trifluoroethyl methacrylate 40.0g and hydroxyethyl methylacrylate 7.5g is slowly added to, at a high speed Mechanical agitation pre-emulsification 30 minutes, obtains 93.7g pre-emulsion II.
In reaction unit nitrogen atmosphere is kept, 80.0g pre-emulsion I are taken, stirred under 200 revs/min, open condensation Water, is heated to 80 DEG C.After temperature stabilization, remaining pre-emulsion I is slowly added dropwise, rear insulation reaction is dripped 1.5 hours, Obtain seed emulsion.
The Deca pre-emulsion II on the basis of the seed emulsion of above-mentioned acquisition, reaction mixing speed are 175 revs/min, temperature Degree control is incubated 2.0 hours after dripping, stopped reaction at 80 DEG C.Emulsion is cooled to into 35 DEG C, Deca 2.0g ammonia adjusts pH value For 7.8, nitrogen, condensed water are closed, 335.85g emulsions are filtered to obtain.
Embodiment 2
By deionized water 340.0g, dodecylbenzene sodium sulfonate 4.8g, fatty alcohol-polyoxyethylene ether 4.8g, 2- acryloyl After amine -2- methyl propane sulfonic acid sodium salt 6.4g, potassium peroxydisulfate 2.25g stirring and dissolving, ethyl methacrylate is slowly added to The mixed liquor of 170.0g, ethyl acrylate 138.0g and hexafluorobutyl acrylate 22.0g, high speed machine stirring pre-emulsification 1 hour, Obtain 666.25g pre-emulsion I.
By deionized water 70g, dodecylbenzene sodium sulfonate 0.68g, fatty alcohol-polyoxyethylene ether 1.36g, 1.0g persulfuric acid After potassium stirring and dissolving, the mixed liquor of hexafluorobutyl acrylate 58.0g and methacrylonitrile 19.2g is slowly added to, high speed machine is stirred Mix pre-emulsification 45 minutes, obtain 149.24g pre-emulsion II.
In reaction unit nitrogen atmosphere is kept, 225.0g pre-emulsion I are taken, stirred under 250 revs/min, opened cold Solidifying water, is heated to 75 DEG C.After temperature stabilization, remaining pre-emulsion I is slowly added dropwise, insulation reaction is dripped 2.0 hours, Obtain seed emulsion.
The Deca pre-emulsion II on the basis of the seed emulsion of above-mentioned acquisition, reaction mixing speed are 225 revs/min, temperature Degree control is incubated 3.0 hours after dripping, stopped reaction at 75 DEG C.Emulsion is cooled to into 40 DEG C, 5% sodium bicarbonate solution of Deca 10.0g, adjusts pH value to be 8.2, closes nitrogen, condensed water, filter to obtain 818.64g emulsions.
Embodiment 3
By deionized water 165.0g, 1,2- dodecyl diether disulfonate 1.6g, NPE 2.0g, After alkyl phenol allyl polyether sulfate 2.2g, sodium peroxydisulfate 1.35g stirring and dissolving, butyl methacrylate is slowly added to The mixed liquor of 70.0g, Process Conditions of Cetane Acrylate 90.0g and perluorooctyl acrylate 10.0g, high speed machine 30 points of pre-emulsification of stirring Clock, obtains 332.15g pre-emulsion I.
By deionized water 40.0g, 1,2- dodecyl diether disulfonate 0.7g, NPE 0.7g, After 0.40g sodium peroxydisulfate stirring and dissolving, be slowly added to perluorooctyl acrylate 28.0g, N hydroxymethyl acrylamide 8.5g with The mixed liquor of methacrylic acid 3.0g, high speed machine stirring pre-emulsification 45 minutes, obtains 80.9g pre-emulsion II.
In reaction unit nitrogen atmosphere is kept, 100.0g pre-emulsion I are taken, stirred under 225 revs/min, opened cold Solidifying water, is heated to 78 DEG C.After temperature stabilization, remaining pre-emulsion I is slowly added dropwise, insulation reaction is dripped 1.0 hours, Obtain seed emulsion.
The Deca pre-emulsion II on the basis of the seed emulsion of above-mentioned acquisition, reaction mixing speed are 200 revs/min, temperature Degree control is incubated 2.0 hours after dripping, stopped reaction at 78 DEG C.Emulsion is cooled to into 20 DEG C, 5% potassium hydrogen phosphate of Deca 8.5g, adjusts pH value to be 8.5, closes nitrogen, condensed water, filter to obtain 415.50g emulsions.
Embodiment 4
By deionized water 460.0g, decyl polyoxyethylene ether monomester succinate disodium sulfonate salt 3.75g, fatty alcohol polyoxy second It is after alkene ether 3.50g, allyloxy NPE ammonium sulfate 6.25g, Ammonium persulfate. 3.75g stirring and dissolving, slow to add Enter the mixed liquor of lauryl methacrylate 220.0g and lauryl acid esters 200.0g, high speed machine stirring pre-emulsification 1 Hour, obtain 897.25g pre-emulsion I.
By deionized water 110g, decyl polyoxyethylene ether monomester succinate disodium sulfonate salt 1.15g, aliphatic alcohol polyethenoxy After ether 1.05g, Ammonium persulfate. 1.5g stirring and dissolving, perfluoro butyl ethyl propylene acid esters 96.0g, N- methylol propylene is slowly added to The mixed liquor of amide 9.5g and hydroxyethyl methylacrylate 18.5g, high speed machine stirring pre-emulsification 1 hour, obtains 236.2g pre- Emulsion II.
In reaction unit nitrogen atmosphere is kept, 300.0g pre-emulsion I are taken, stirred under 300 revs/min, opened cold Solidifying water, is heated to 82 DEG C.After temperature stabilization, remaining pre-emulsion I is slowly added dropwise, insulation reaction is dripped 2.5 hours, Obtain seed emulsion.
The Deca pre-emulsion II on the basis of the seed emulsion of above-mentioned acquisition, reaction mixing speed are 250 revs/min, temperature Degree control is incubated 3.0 hours after dripping, stopped reaction at 82 DEG C.Emulsion is cooled to into 25 DEG C, 5% potassium carbonate 12.5g of Deca, Adjust pH value to be 8.0, close nitrogen, condensed water, filter to obtain 1138.84g emulsions.
Embodiment 5
By deionized water 600.0g, NPE ammonium sulfate 5.0g, OPEO 8.0g, allyl After base polyethers sulfate 8.0g, Ammonium persulfate. 1.8g stirring and dissolving, octadecyl methacrylate 225.0g and propylene are slowly added to The mixed liquor of the different monooctyl ester 275.0g of acid, high speed machine stirring pre-emulsification 30 minutes, obtains 1122.8g pre-emulsion I;
By deionized water 175.0g, NPE ammonium sulfate 2.6g, OPEO 4.2g, over cure After sour ammonium 0.9g stirring and dissolving, perfluoro hexyl ethylmethyl acrylate 185.0g and Hydroxypropyl methacrylate are slowly added to The mixed liquor of 40.5g, high speed machine stirring pre-emulsification 30 minutes, obtains 408.2g pre-emulsion II.
In reaction unit nitrogen atmosphere is kept, 380.0g pre-emulsion I are taken, stirred under 300 revs/min, opened cold Solidifying water, is heated to 80 DEG C.After temperature stabilization, remaining pre-emulsion I is slowly added dropwise, rear insulation reaction 2.0 is dripped little When, obtain seed emulsion.
The Deca pre-emulsion II on the basis of the seed emulsion of above-mentioned acquisition, reaction mixing speed are 250 revs/min, temperature Degree control is incubated 5.0 hours after dripping, stopped reaction at 80 DEG C.Emulsion is cooled to into 30 DEG C, 5% dipotassium hydrogen phosphate of Deca 18.5g, adjusts pH value to be 8.4, closes nitrogen, condensed water, filter to obtain 1518.7g emulsions.
Embodiment 6
Emulsion paint will be configured to by embodiment of the present invention 1-5 emulsion to be detected, detection project is shown in Table 1, testing standard is HG/T4104-2009。
Table 1 prepares the specific performance of emulsion

Claims (11)

1. a kind of preparation method of fluorinated acrylate emulsion, is characterized in that comprising the steps of:
1) prepare pre-emulsion
I) the preparation of core pre-emulsion
After anion emulsifier, nonionic emulsifier, reactive emulsifier, initiator and deionized water stirring and dissolving, add With or without the methacrylate-based monomer and acrylic ester monomer mixed liquor of fluoroalkyl class monomer, stirring is pre- Emulsifying prepares core pre-emulsion, and wherein each component mass parts are:
II) the preparation of shell pre-emulsion
After anion emulsifier, nonionic emulsifier, initiator and deionized water stirring and dissolving, add containing perfluoroalkyl acrylic Esters monomer and the mixed solution of functional monomer, stir pre-emulsification and prepare shell pre-emulsion, and wherein each component mass parts are:
2) preparation of seed emulsion
Take step 1) obtained by the 20-50% of core pre-emulsion stir under inert gas shielding, be warming up to 70-90 DEG C, treat temperature After stable, residual nucleus emulsion is dripped, afterwards insulation reaction, seed emulsion is obtained;
3) prepare fluorinated acrylate emulsion
Be kept stirring for, inert gas shielding, temperature are maintained under the conditions of 70-90 DEG C, to step 2) obtained by seed emulsion drip Step 1) obtained by shell pre-emulsion, drop finishes insulation reaction, after reaction completely, is down to 10-30 DEG C, and Deca pH adjusting agent to pH value is 7.0-8.5, mixed liquor filters to obtain fluorinated acrylate emulsion;
The anion emulsifier is selected from sodium lauryl sulphate, dodecylbenzene sodium sulfonate, two sulphur of 1,2- dodecyls diether Acid disodium, decyl polyoxyethylene ether monomester succinate disodium sulfonate salt, NPE ammonium sulfate, polyoxyethylene nonyl phenyl second Alkene ether monomester succinate disodium sulfonate salt or polyoxyethylenated alcohol sodium sulfate;
The nonionic emulsifier is selected from fatty alcohol-polyoxyethylene ether, OPEO or NPE.
2. preparation method according to claim 1, it is characterised in that the acrylic ester monomer is selected from acrylic acid first Ester, ethyl acrylate, butyl acrylate, Isooctyl acrylate monomer, Process Conditions of Cetane Acrylate or octadecyl acrylate.
3. preparation method according to claim 1, it is characterised in that the methacrylate-based monomer is selected from methyl-prop E pioic acid methyl ester, ethyl methacrylate, butyl methacrylate, lauryl methacrylate or octadecyl methacrylate.
4. preparation method according to claim 1, it is characterised in that the fluorine-containing alkylacrylate monomer is Formulas I Compound
Wherein R1Selected from H or methyl, R2Selected from C2-C20Containing fluoroalkyl.
5. preparation method according to claim 4, it is characterised in that the fluorine-containing alkylacrylate monomer is selected from first Base acrylic acid trifluoro ethyl ester, hexafluorobutyl acrylate, perluorooctyl acrylate, dodecafluoroheptyl methacrylate, perfluor fourth Base ethyl propylene acid esters, perfluoro butyl ethylmethyl acrylate, perfluoro hexyl ethylmethyl acrylate, perfluorooctylethyl group Acrylate or perfluorooctylethyl group methacrylate.
6. preparation method according to claim 1, it is characterised in that the functional monomer is selected from methacrylic acid, first Base 2-(Acryloyloxy)ethanol, Hydroxypropyl methacrylate, methacrylonitrile, acrylic acid, 2-(Acryloyloxy)ethanol, Hydroxypropyl acrylate, Acrylonitrile, acrylamide, N hydroxymethyl acrylamide, Ethylene glycol dimethacrylate or N-[2-(2-methyl-4-oxopentyl) or its group Close.
7. preparation method according to claim 1, it is characterised in that the reactive emulsifier selected from 2- propenyl ethers- 3- hydroxy propane -1- sodium sulfonates, alkyl phenol allyl polyether sulfate, 2- acrylamide -2- methyl propane sulfonic acid sodium salts, allyl Epoxide NPE ammonium sulfate, sodium vinyl sulfonate, allyl polyether sulfate or allyloxy fatty alcohol oxygen second Alkene ether ammonium sulfate.
8. preparation method according to claim 1, it is characterised in that the initiator is persulfate.
9. preparation method according to claim 8, it is characterised in that the persulfate is selected from sodium peroxydisulfate, persulfuric acid Potassium or Ammonium persulfate..
10. preparation method according to claim 1, it is characterised in that the pH adjusting agent is selected from ammonia, alkali-metal carbon Hydrochlorate, bicarbonate, phosphate or hydrophosphate.
11. preparation methoies according to claim 1, it is characterised in that the pH adjusting agent is selected from ammonia, sodium carbonate, carbon Sour hydrogen sodium, disodium hydrogen phosphate, potassium carbonate, potassium hydrogen phosphate or dipotassium hydrogen phosphate.
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