CN1122812A - Prepn. method of water soluble sulfonated phenylethylene copolymer - Google Patents

Abstract

The water-soluble sulfonated styrene co-polymer used as anti-encrustation disperser in industrial water conditioning is prepared by water-phase suspension polymerization of styrene and acrylonitrile useing a larger amount of initiator and after polymerization, is needed, no drying is needed, and the co-polymer undergoes sulfonated-hydrolysis directly with concentrated sulfuric acid to obtain water-soluble resultant. Advantages: low cost, good anti-encrustation, high heat-stability and can be used as slurry thinner in petroleum deep-well drilling.

Description

The method for making of water soluble sulfonated phenylethylene copolymer

The present invention relates to the method for making of Treatment of Industrial Water medicament, exactly, is relevant dirt dispersion agent--the method for making of-water soluble sulfonated phenylethylene copolymer.

At first found styrene sulfonic acid and acrylic copolymer since the dirt dispersion agent (seeing U.S. Pat 4048066) as water system since 1977, three international water at the beginning of the eighties can be gone up, all relevant for the paper publishing of sulfonated phenylethylene copolymer, particularly the 41st water can the relevant paper phosphorus that is developed as of estimating sulfonic acid copolymer be that the prescription of water treatment agent has been opened up new world.Other sulfonic acid classes: as vinyl sulfonic acid, propene sulfonic acid, 2-methyl-2-acrylamido propyl sulfonic acid etc. also occur in succession, the common trait of sulfonic acid analog copolymer water treatment agent is that sulfonic acid is more stable under the high pH value of high temperature, scale-inhibiting properties is good, especially hinders the multipolymer that calcium phosphate scale and iron dirt are much better than former vinylformic acid and ester class thereof.

The styrene sulfonic acid multipolymer can be by monomer whose and other monomers such as vinylformic acid polymerization in homogeneous phase and getting in the aqueous solution, or can by vinylbenzene and other monomers such as maleic anhydride in organic solvent copolymerization through separating sulfonation again, hydrolysis makes the multipolymer of sulfonated phenylethylene and toxilic acid.Preceding method makes product cost too high because the styrene sulfonic acid monomer costs an arm and a leg; Back one method then can not make sulfonated vinylbenzene and acrylic copolymer, even because of preparing separable vinylbenzene and acrylic copolymer, and when using concentrated acid sulfonation, acrylic acid segment place easily is carbonized.Japanese Patent JP 8225302 once proposed the multipolymer that available 95% sulfuric acid sulfonation contains 75% vinylbenzene and 25% vinyl cyanide, with the preparation water regain be resin from 40 times of heights water-swellable polymer, as water-loss reducer of soil etc.

Purpose of the present invention, just be to provide a kind of cheaply, have a method for making of the water soluble sulfonated phenylethylene copolymer of high scale inhibition performance and high thermal stability.

Used for reference the reaction principle of above-mentioned Japanese Patent, consider the hydrolysis property that vinyl cyanide has, and acrylamide also is the reality of one of water treatment agent copolymerization component commonly used, the present invention has adopted the aqueous suspension polymerization technology, selected higher initiator amount scope especially, prepare earlier and meet the scale-inhibiting properties requirement (molecular weight is little, relative viscosity is low) special-purpose styrene-acrylonitrile copolymer, carry out the sulfonation hydrolysis reaction under given conditions with the suitable vitriol oil of concentration again, directly obtain a kind of sulphuric acid soln product of heavy-gravity sulfonated phenylethylene copolymer.Application shows, this product water soluble is a kind of Scale inhibitors that high scale inhibition performance and high thermal stability are arranged in Treatment of Industrial Water, in oil production, can be used as the slurry thinner of deep drilling exploration.Present cost analysis shows that the method for expense of raw materials contrast styrene sulfonic acid monomer polymerization of the present invention will reduce many.

Technological process of the present invention is: making 5--32% earlier (is 10--26% preferably; for the suspension system gross weight; vinylbenzene down together) and the vinyl cyanide of 4--12% (being preferably 5--10%) are in aqueous phase suspension polymerization; with the active calcium phosphate is suspension agent; consumption is 0.05--1.0% (being preferably 0.1--0.5%); with Potassium Persulphate (or ammonium) is promotor; consumption is 0.01--0.2%; with dibenzoyl peroxide or Diisopropyl azodicarboxylate is initiator; consumption is 0.05--8% (being preferably 1-5%), and surplus is a water.At 75-100 ℃ of polymerization 2-10 hour, filtering filtrate can be recycled after transferring ph, resin can be without (or warp) drying, directly with the sulfuric acid of concentration 82-95% in 80-160 ℃ (being preferably 110-140 ℃) hydrolysis sulfonation 2-13 hour (being preferably 3-7 hour) down, this moment the dried resin charging capacity to account for sulfonation system weight ratio be 2.5--13% (being preferably 8.5--12.5%).Finally make thick brown sulfonated phenylethylene copolymer sulphuric acid soln.

Process characteristic of the present invention is: the amount of initiator of selecting for use in the suspension polymerization is higher, to make the low-molecular weight copolymer of scale inhibition requirement, makes its relative viscosity lower; Be need not reclaim a small amount of unreacted monomer after the polymerization in addition, the suspension polymerization medium is adjusted after the ph value (8-9) promptly reusable with sodium hydroxide; Resin can be dry, and available one step of sulfuric acid is finished hydrolysis reaction; Sulfuric acid no longer removes in the product.This product is because of containing the Phenylsulfonic acid side group in its multipolymer, so Heat stability is good than other sulfonic acid, simultaneously, also contain the vinylformic acid chain link in the multipolymer, and vinylformic acid is than the Heat stability is good (IWC-82-37) of toxilic acid, so the thermostability of this product is better than styrene sulfonic acid and maleic acid.Confirm with Infrared spectroscopy in the research, really contain amide group in the multipolymer of the present invention, and find most itrile group only hydrolysis till the amide group, illustrate that this product is different with vinylbenzene sulphur sulfonic acid and acrylic copolymer, final product comes down to a kind of terpolymer based on styrene sulfonic acid and acrylamide two components, and it is worthy of the name being referred to as " sulfonated phenylethylene copolymer ".

In following examples, selected suspension agent active calcium phosphate is only formulated by Sodium phosphate dibasic and calcium chloride, and tertiary sodium phosphate replaces the Sodium phosphate dibasic effect identical, must adjust ph (8-10) value when using SODIUM PHOSPHATE, MONOBASIC.Separate and dry resulting polymers resin after the suspension polymerization in the example, and sulfonation after removing steps such as sulfuric acid, water isolation all is for chemico-analytic convenience.

The relative viscosity index is solvent with the dimethyl formamide in the example, and concentration is 1g resin/100ml solution, measures down at 25 ℃.The condition of measuring calcium phosphate scale, calcium carbonate scale, ironic hydroxide dirt scale inhibition performance is as shown in the table.Dosage is in effective constituent in the table.Test back water sample is with filter paper filtering, respectively with the blue spectrophotometry of phosphorus molybdenum

Estimate the test conditions of various scale inhibition performance Y

The dirt type	??Ca 3(PO 4) 2	???CaCO 3	?????Fe(OH) 3
				Dosage (PPM)	????7	????10	???????5
Ca 2+(PPM)	????100	????100	??????120
				Mg 2+(PPM)	????/	????/	??????72
HCO 3 -(mmol/l)	????/	????5	???????3
				PO 4 3-(PPM)	????6	????/	???????/
Fe 3+(PPM)	????/	????/	???????3
				Borax (PPM)	????1000	????/	???????/
PH	????9.0	????9.0	?????7.0
				Temperature (℃)	????80	????80	??????30
Time (h)	????10	????10	???????2

Survey PO ₄ ^3-, survey Ca with complexometry ²⁺, with sulphosalicylic acid spectrophotometry Fe ³⁺Each scale inhibition performance Y calculates with following formula: $Y=\frac{x_2-x_0}{x_1-x_0}\×100\%$ In the formula: x ₂Be institute's measured ion concentration in the test rear filtrate;

x ₁Be institute's measured ion concentration in the water sample before testing;

x ₀Be institute's measured ion concentration in the test of the adding medicine not rear filtrate.

Embodiment 1

Be furnished with at 250ML and add the 132.3g deionized water in the there-necked flask of condenser and agitator, start stirring, add the 0.13g Sodium phosphate dibasic, add the 0.31g Calcium Chloride Powder Anhydrous after the dissolving again, add the 0.02g ammonium persulphate after 5 minutes, add 42.9g vinylbenzene at last, 18.4g vinyl cyanide and 6.0g dibenzoyl peroxide, stir revolution and mention about 400 rev/mins, be warmed up to 78 ℃, can reach about 90 ℃, can reach 100 ℃ through one hour temperature again through one hour temperature, note remaining trace and reflux, and be incubated one hour.Cooling then, discharging, filtration, drying get the 62.0g resin.Relative viscosity is 1.328.Take by weighing the 30g resin and add and to be equipped with in the 210g86% concentration vitriolic 250ML there-necked flask, open to be stirred in one hour and be warmed up to 130-140 ℃, hydrolysis sulfonation 5 hours, cooling discharging, the red-brown thick liquid.Product with Infrared spectroscopy, is found at 1668cm after water isolation is removed sulfuric acid ^-1, 1040cm ^-1And 837cm ^-1There is obvious absorption peaks at the place, and does not have phenyl ring and the appearance of itrile group characteristic peak, i.e. all sulfonation of phenyl ring, all hydrolysis of itrile group.With the ammonium content in the nessler reagent spectrophotometry product, find to have only 42% itrile group depth hydrolysis to be carboxyl, all the other only are hydrolyzed to amide group, and are consistent with Infrared spectroscopy.

The scale inhibition performance of sampling and measuring calcium phosphate, lime carbonate, ironic hydroxide dirt is respectively 80.8%, 37.7%, 84.0%.Replace mud with titanium dioxide powder and water preparation slurries, wherein contain TiO ₂40% at room temperature measures viscosity (in second) with being coated with-4 glasss, when this product to TiO ₂Amount is respectively 0,1%, 2%, 3%, and 4% o'clock, viscosity was followed successively by 73.6,60.9,53.0,49.6,81.9 seconds.

Embodiment 2

Remove the polymerization feeding quantity and change vinylbenzene 20.1g into, vinyl cyanide 10.7g, dibenzoyl peroxide 1.5g, outside the water 167.3g, other are with embodiment 1.The resin 27.2g that must do, relative viscosity 1.339.Except that sulfuric acid concentration changes 82% into, the hydrolysis sulfonation time changes into 9 hours, other hydrolysis sulfonation conditions are with embodiment 1, and the calcium phosphate of product and lime carbonate scale inhibition performance are respectively 61.6% and 50.7%.

Embodiment 3

The polymerization feeding quantity changes vinylbenzene 53.5g into, vinyl cyanide 17.8g, Sodium phosphate dibasic 0.55g, Calcium Chloride Powder Anhydrous 0.82g, Potassium Persulphate 0.2g, dibenzoyl peroxide 10.5g, water 116.6g; Polymerization time shortens to 2.5 hours, and other are operated with embodiment 1, gets dried resin 73g, relative viscosity 1.288.Take by weighing the 20g resin and add in the sulfuric acid of 180g95%, 110--120 ℃ of hydrolysis sulfonation temperature, the reaction times is three hours, other behaviour do with embodiment 1.The calcium phosphate of product and calcium carbonate scale scale inhibition performance are respectively 65.4% and 41.0%.

The present invention utilizes the aqueous suspension polymerization technology to prepare vinylbenzene and acrylonitrile copolymer, and warp and sulfuric acid reaction can make phenyl ring sulfonation, itrile group hydrolysis simultaneously, is the novel method of a low-cost preparation water soluble sulfonated phenylethylene copolymer.And non-wastewater discharge in the preparation process.Product of the present invention has excellent resistance ironic hydroxide dirt, resistance calcium phosphate scale performance, with the organic phosphine acids synergistic effect is arranged, and can be used for recirculated cooling water and middle low-pressure boiler uses water as dirt dispersion agent; This product also can reduce mud viscosity, because its good thermostability, so in deep drilling exploration, can make slurry thinner.

Claims (6)

1. a Treatment of Industrial Water is with the method for making of dirt dispersion agent-water soluble sulfonated phenylethylene copolymer, it is characterized in that: make 5-32% earlier (for the suspension system gross weight, vinylbenzene down together) and the vinyl cyanide of 4-12% are in aqueous phase suspension polymerization, with the active calcium phosphate is suspension agent, consumption is 0.05-1.0%, with Potassium Persulphate (or ammonium) is promotor, consumption is 0.01--0.2%, with dibenzoyl peroxide or Diisopropyl azodicarboxylate is initiator, consumption is 0.05--8%, surplus is a water, at 75-100 ℃ of polymerization 2-10 hour, filtering rear filtrate can be recycled through transferring the ph value, resin is drying (or drying) not, 80-160 ℃ of following hydrolysis sulfonation 2-13 hour, the dried resin charging capacity accounted for sulfonation system weight ratio and should be 2.5-13% this moment, finally made water miscible thick brown sulfonated phenylethylene copolymer sulphuric acid soln with the sulfuric acid of concentration 82-95%;

2. by the described method for making of claim 1, it is further characterized in that the better amount that adds vinylbenzene and vinyl cyanide in the aqueous suspension polymerization system is respectively 10-26% and 5-10%;

3. by the described method for making of claim 1, it is further characterized in that in the aqueous suspension polymerization system, add the suspension agent active calcium phosphate better amount be 0.1--0.5%, add initiator dibenzoyl peroxide or Diisopropyl azodicarboxylate better amount be 1-5%;

4. by the described method for making of claim 1, it is further characterized in that the better temperature of reaction of hydrolysis sulfonated is 110--140 ℃, and better the reaction times is 3-7 hour, this moment the dried resin charging capacity to account for the better ratio of sulfonation system weight be 8.5--12.5%;

5. by the described method for making of claim 1, after it is further characterized in that aqueous suspension polymerization, filters filtrate and after sodium hydroxide adjusting ph is 8-9, can be recycled.

6. the product of this law preparation is applicable to that recirculated cooling water and middle low-pressure boiler use water as Scale inhibitors, is applicable to that also the oil deep drilling exploration makes slurry thinner.