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CN1458177A - Technology for preparing itaconic acid-propenoic acid copolymer from fermented liquid - Google Patents

Technology for preparing itaconic acid-propenoic acid copolymer from fermented liquid Download PDF

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Publication number
CN1458177A
CN1458177A CN 02110331 CN02110331A CN1458177A CN 1458177 A CN1458177 A CN 1458177A CN 02110331 CN02110331 CN 02110331 CN 02110331 A CN02110331 A CN 02110331A CN 1458177 A CN1458177 A CN 1458177A
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CN
China
Prior art keywords
acid
itaconic acid
technology
acid copolymer
propenoic
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CN 02110331
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Chinese (zh)
Inventor
赵立新
董风波
马长友
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ZIBO MINING GROUP CO Ltd
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ZIBO MINING GROUP CO Ltd
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Priority to CN 02110331 priority Critical patent/CN1458177A/en
Publication of CN1458177A publication Critical patent/CN1458177A/en
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Abstract

The present invention provides technology of preparing itaconic acid-propenoic acid copolymer from fermented liquid. With the fermented liquid for producing itaconic acid via biological fermentation as material, and through ionic exchange, concentration, copolymerization with propenoic acid in the presence of initiator, itaconic acid-propenoic acid copolymer solution is prepared. Using the fermented liquid as initial material can lower the cost greatly, and the free radical polymerization process solves the demerit of hard homopolymerization of itaconic acid. The process has less residual monomer and high conversion rate. The copolymer may be used as scale inhibitor, scale remover, dispersant, detergent assistant, etc.

Description

The technology for preparing itaconic acid-propenoic acid copolymer by the fermentation soup
Technical field
The present invention relates to the technology of methylene-succinic acid and acrylic acid copolymer, specifically is the technology that is prepared itaconic acid-propenoic acid copolymer by the fermentation soup.
Background technology
The domestic report of relevant process for polymerization of itaconic acid is less, and the difficult homopolymerization of methylene-succinic acid is in common knowledge for everybody.In addition, the higher development that limits its purposes of methylene-succinic acid price.As the invention disclosed patent application on October 14 in 1992 of Chinese patent communique: process for polymerization of itaconic acid, application number: 92102091, its technical scheme is: be placed with in the container of water when complete neutral monomer solution and initiator solution are joined beginning, be enough to carry out promptly can to generate the polymerization of itaconic acid thing by high conversion under the temperature of polyreaction, transformation efficiency is higher, but owing to consume a large amount of alkali cost is raise.
The production of relevant polycarboxylic acid polymkeric substance both at home and abroad and use morely as polyacrylic acid, hydrolytic polymaleic anhydride, vinylformic acid-maleic acid etc., is widely used in Scale inhibitors, dispersion agent, washing auxiliary detergent, chela and agent etc.Because hydrolytic polymaleic anhydride needs polymerization in organic solvent, pollute greatlyyer, and domestic its polymericular weight is less, someone studies vinylformic acid and toxilic acid aqueous solution copolymerization, and carboxyl is than polyacrylic acid content height on its polymer chain, and is better dispersed, and chela and calcium, magnesium value are higher, reach 200mg/g as the calcium chelating value, pollute also for a short time, but from reactivity ratio, vinylformic acid is 18.05, toxilic acid is 0.0085, and polymerization effect is bad.
Summary of the invention
Characteristics of the present invention are that with the fermentation soup in the methylene-succinic acid production be starting raw material, reduce its cost greatly, and the characteristics of the difficult homopolymerization of methylene-succinic acid have been solved with acrylic acid copolymer, transformation efficiency is higher, its reactivity ratio is respectively: vinylformic acid is 1.89, methylene-succinic acid is 0.52, and polymerization effect is good, carboxylic acid group's content height on the molecular chain.
Concrete grammar of the present invention is: the fermentation soup of producing in the methylene-succinic acid with biological fermentation process is a raw material, after ion-exchange, concentrating, carries out copolymerization with vinylformic acid in the presence of initiator, prepares itaconic acid-propenoic acid copolymer solution.
The described technology for preparing itaconic acid-propenoic acid copolymer by the fermentation soup, the itaconic acid fermentation soup is passed through ion exchange column, remove magnesium wherein, zinc and other metal ion, after to be concentrated into the methylene-succinic acid mass content be 5%~40%, join in the reactor under the insulation, steady temperature is between 30~100 ℃, add initiator solution with uniform feed rate, vinylformic acid, wherein active initiator content (is benchmark with the monomer mass) is 0%~20%, vinylformic acid (is benchmark with the methylene-succinic acid quality) add-on is 5%~200%, add material back restir for some time, about 0.5~3 hour, prepare itaconic acid-propenoic acid copolymer solution.
Describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, the fermentation soup also can concentrate earlier, after pass through ion exchange column.
Describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, initiator is selected from the combination of following wherein one or more oxygenants: Sodium Persulfate, ammonium persulphate, Potassium Persulphate, peroxophosphoric acid sodium, potassium superphosphate, ammonium superphosphate, hydrogen peroxide and tert-butyl peroxide, diacyl peroxide; Or itself and single the kind or the combination of multiple reductive agent: sulphite, hydrosulphite, phosphite, thiosulphate, sulfurous acid, mercaptan, ferrous salt, amine are (as N, accelerine) etc., with oxygenant or and the water-soluble respectively aqueous solution that is prepared into of reductive agent, form initiator system.Its concentration is 0.5~30%.Suitable oxygenant is a persulphate, evenly adds in polyreaction, and reductive agent is sulphite, thiosulphate, ferrous salt.
Describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, the reductive agent in the initiator can join before polymerization in the methylene-succinic acid solution, also can evenly add in the reaction system in polymerization.
Describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, initiator and acrylic acid reinforced time are 0.5~5 hour.
The described technology for preparing itaconic acid-propenoic acid copolymer by the fermentation soup, the itaconic acid-propenoic acid copolymer solution of gained is the liquid of solid content about 5%~80%, but also behind the concentrate drying sheet or powdery solid, available bases is (as sodium hydroxide, potassium hydroxide, ammonia etc.) after the neutralization, the reconcentration drying is sheet or powdery solid.
According to initiator and other condition difference,, be fit to different purposes by the inventive method synthetic polymkeric substance for molecular weight is 300~20000 series product (number-average molecular weight).This polymkeric substance can be used for Scale inhibitors, scale remover, sequestrant, dispersion agent, washing auxiliary detergent etc.This polymkeric substance has good dispersing property to ferric oxide etc., can effectively stop the formation of dirts layers such as lime carbonate, magnesiumcarbonate, silicate, hydroxylapatite and adheres to, and the calcium chelating value can reach more than the 240mg/g, and the magnesium chelating value can reach more than 200.
Embodiment
Example 1: a certain amount of itaconic acid fermentation soup is passed through cationic exchange coloum, the back is concentrated into solid content under negative pressure be 35% methylene-succinic acid solution, get this solution 300mL and join in the 500mL four-hole round-bottomed flask, get ferrous sulfate 0.1g and add wherein dissolving, and feed nitrogen.Respectively 4g Sodium Persulfate and 4g S-WAT are dissolved in the 50mL water, 90 ℃ down and 70g vinylformic acid join simultaneously in the flask, add restir 1 hour in 3 hours.Cooling obtains 392mL scarlet polymers soln.
Resulting polymers solution transformation efficiency is 97.8% (is benchmark with the methylene-succinic acid), and unpolymerized remaining methylene-succinic acid monomer is 2.2%.Resulting polymers density is 1.21g/mL (25 ℃), and solid content is 42.3%, and number-average molecular weight is 900.
The test of resulting polymers scale inhibition performance: contain Ca 2+250mg/L, HCO 3 -250mg/L (in lime carbonate) hard water preparation: get NaHCO 30.21g and CaCl 20.2775g be dissolved in the 200mL distilled water, be diluted with water to 1000mL.This polymkeric substance and commercially available hydrolytic polymaleic anhydride are joined respectively in this hard water of 500mL, making its effective constituent concentration is 8mg/L, stirs 8 hours cooled and filtered down at 80 ℃, with calcium contents in the EDTA filtrates tested, scale inhibition performance is respectively 99.80% and 99.75%.
The test of resulting polymers dispersing iron oxide: get 0.0880gFeSO 47H 2O, 100mL0.25mol/L Na 2B 4O 7, 40.8mL1mol/LHCl is made into 2000mL solution, and wherein polymkeric substance effective constituent is 10mg/L, and 70 ℃ of following constant temperature 6 hours, cooling was left standstill.Getting this polymkeric substance equally compares with commercially available hydrolyzed polymaleic anhydride, the cooling back adds the solution non-oxidation iron precipitation of this polymkeric substance, is 88.7% with spectrophotometer at 650nm place its transmittance of test, and the solution of adding polymaleic acid has a large amount of red iron oxides precipitations, and its transmittance is 100%.
Example 2: by cationic exchange coloum, the back is concentrated into solid content under negative pressure be 39% methylene-succinic acid solution with a certain amount of itaconic acid fermentation soup, gets this solution 300mL and join in the 500mL four-hole round-bottomed flask, and feed nitrogen.Respectively 4g Sodium Persulfate and 6g S-WAT are dissolved in the 50mL water, 70 ℃ down and 80g vinylformic acid join simultaneously in the flask, add restir 1 hour in 2 hours.Cooling obtains the faint yellow polymers soln of 405mL.
Resulting polymers solution transformation efficiency is 99.7% (is benchmark with the methylene-succinic acid), and unpolymerized remaining methylene-succinic acid monomer is 0.3%.Resulting polymers density is 1.19g/mL (25 ℃), and solid content is 41.6%, and number-average molecular weight is 2000.
Resulting polymers is stung the test of the value of closing: get a certain amount of polymkeric substance, solid content is about 0.2g, add water 100mL, regulate pH to 10 with sodium hydroxide, get 20mL0.05M calcium chloride and add, and be diluted to 250mL, in 35 ℃ of following constant temperature 20 minutes, cooled and filtered is got filtrate analysis, and calculating the calcium chelating value is 256mg/g.To sting the value of closing be 180mg/g with record magnesium with quadrat method.
The application of gained multipolymer aspect Scale inhibitors, scale remover, dispersion agent and washing auxiliary detergent, more specifically saying so with soup in the itaconic acid fermentation production is raw material, after ion-exchange, concentrating, the polymkeric substance that makes with this method is fit to do Scale inhibitors, dispersion agent, scale remover, washing auxiliary detergent etc.
Describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, the methylene-succinic acid finished product can be mixed with 5%~40% the aqueous solution, carries out copolymerization.

Claims (10)

1, a kind of technology for preparing itaconic acid-propenoic acid copolymer by the fermentation soup, it is characterized in that: the fermentation soup of producing in the methylene-succinic acid with biological fermentation process is a raw material, after ion-exchange, concentrating, in the presence of initiator, carry out copolymerization, prepare itaconic acid-propenoic acid copolymer solution with vinylformic acid.
2, as claimed in claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer, it is characterized in that adopting following steps by the fermentation soup:
(a) the fermentation soup of biological fermentation process being produced in the methylene-succinic acid passes through ion exchange column, removes wherein metal ion such as magnesium, zinc;
(b) aforesaid liquid is evaporated to contain the methylene-succinic acid amount be 5%~40%;
(c) add initiator solution, vinylformic acid with uniform feed rate, wherein active initiator content (is benchmark with the monomer mass) is 0%~20%, and vinylformic acid (is benchmark with the methylene-succinic acid quality) add-on is 5%~200%
(d) entire reaction course maintains the temperature at 30~100 ℃, reacts 0.5~3 hour after adding material again, prepares itaconic acid-propenoic acid copolymer solution.
3, according to claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, it is characterized in that: the fermentation soup also can concentrate earlier, after pass through ion exchange column.
4, according to claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, it is characterized in that: initiator is selected from the combination of following wherein one or more oxygenants: Sodium Persulfate, ammonium persulphate, Potassium Persulphate, peroxophosphoric acid sodium, potassium superphosphate, ammonium superphosphate, hydrogen peroxide and tert-butyl peroxide, diacyl peroxide; Or itself and single the kind or the combination of multiple reductive agent: sulphite, hydrosulphite, phosphite, thiosulphate, sulfurous acid, mercaptan, ferrous salt, amine (as N, accelerine) etc., wherein oxygenant evenly adds in polyreaction.
5. describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup according to claim 1,4, it is characterized in that: the reductive agent in the initiator joins before polymerization in the methylene-succinic acid solution.
6. describedly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup according to claim 1,4, it is characterized in that: the reductive agent in the initiator evenly adds in the reaction system in polymerization.
7. according to claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, it is characterized in that: initiator and acrylic acid reinforced time are 0.5~5 hour.
8. according to claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer by the fermentation soup, it is characterized in that: the itaconic acid-propenoic acid copolymer solution of gained is the liquid of solid content 5%~80%.
9. according to claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer, it is characterized in that by the fermentation soup: but be sheet or powdery solid behind the itaconic acid-propenoic acid copolymer solution concentrate drying of gained.
10. according to claim 1ly prepare the technology of itaconic acid-propenoic acid copolymer, it is characterized in that by the fermentation soup: the itaconic acid-propenoic acid copolymer solution of gained with in the alkali and after, the reconcentration drying is sheet or powdery solid.
CN 02110331 2002-05-15 2002-05-15 Technology for preparing itaconic acid-propenoic acid copolymer from fermented liquid Pending CN1458177A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105209508A (en) * 2013-03-15 2015-12-30 路博润先进材料公司 Itaconic acid polymers

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105209508A (en) * 2013-03-15 2015-12-30 路博润先进材料公司 Itaconic acid polymers
CN110105480A (en) * 2013-03-15 2019-08-09 路博润先进材料公司 Polymerization of itaconic acid object
JP2020090687A (en) * 2013-03-15 2020-06-11 ルブリゾル アドバンスド マテリアルズ, インコーポレイテッド Itaconic acid polymer
JP7065135B2 (en) 2013-03-15 2022-05-11 ルブリゾル アドバンスド マテリアルズ, インコーポレイテッド Itaconic acid polymer

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