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CN1418883A - Method for producing 1-hydroxy ethylene-1,1-diphosphonic acid - Google Patents

Method for producing 1-hydroxy ethylene-1,1-diphosphonic acid Download PDF

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Publication number
CN1418883A
CN1418883A CN 02137110 CN02137110A CN1418883A CN 1418883 A CN1418883 A CN 1418883A CN 02137110 CN02137110 CN 02137110 CN 02137110 A CN02137110 A CN 02137110A CN 1418883 A CN1418883 A CN 1418883A
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acetic acid
diphosphonic acid
hydroxyethylidene diphosphonic
phosphorus trichloride
reaction
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侯秀峰
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Fudan University
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Fudan University
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Abstract

本发明是一种羟基乙叉二膦酸的生产方法。在100℃~120℃温度下,将三氯化磷直接滴入醋酸中,迅速得到乙酰化的羟基乙叉二膦酸,同时分离和回收乙酰氯和氯化氢。然后通蒸汽水解,回收醋酸,得到羟基乙叉二膦酸溶液。本发明可加快反应速度,缩短反应时间,降低能耗,节约成本,并可提高反应安全性。The invention is a production method of hydroxyethylidene diphosphonic acid. At a temperature of 100°C to 120°C, drop phosphorus trichloride directly into acetic acid to rapidly obtain acetylated hydroxyethylidene diphosphonic acid, and simultaneously separate and recover acetyl chloride and hydrogen chloride. Then steam hydrolysis, recovery of acetic acid, to obtain hydroxy ethylidene diphosphonic acid solution. The invention can accelerate the reaction speed, shorten the reaction time, reduce the energy consumption, save the cost and improve the reaction safety.

Description

一种羟基乙叉二膦酸的生产方法A kind of production method of hydroxyethylidene diphosphonic acid

技术领域technical field

本发明属化工技术领域,具体涉及一种羟基乙叉二膦酸的生产方法。The invention belongs to the technical field of chemical industry, and in particular relates to a production method of hydroxyethylidene diphosphonic acid.

背景技术Background technique

羟基乙叉二膦酸具有良好的络合性和缓冲作用,被广泛的应用工业上,如循环水处理的阻垢剂、金属腐蚀抑制剂和洗涤剂等。羟基乙叉二膦酸的生产方法很多,以三氯化磷和醋酸为原料的合成方法,原料价格较低,操作相对简便,成为目前工业上生产羟基乙叉二膦酸的主要方法。法国专利Fr1521963,在35℃条件下,将三氯化磷加入醋酸和水溶液后,逐渐升温,收集副产物乙酰氯,并将收集的乙酰氯返滴回到反应体系中。该方法须控制在较低的温度下滴加三氯化磷,反应时间长,能耗大。中国专利CN1091137改进了Fr1521963方法中的冷却系统,将收集的副产物乙酰氯加到醋酸溶液中,减少了原料醋酸的消耗。但反应时间长,能耗大。美国专利US3366676提出将三氯化磷加到醋酸和三丁基胺中,反应混合物在封闭容器中加热到136℃。尽管时间很短即可反应完全,但胺的存在影响了产品的纯度。比利时专利Belg.672168在室温下将三氯化磷加入醋酸中,然后缓慢升温至60℃,再升至110℃,分离乙酰化中间产物后,水解得到产品。该方法需要分离乙酰化产物,使操作过程复杂化。Hydroxyethylidene diphosphonic acid has good complexing and buffering effects, and is widely used in industries, such as scale inhibitors for circulating water treatment, metal corrosion inhibitors and detergents. There are many production methods of hydroxyethylidene diphosphonic acid. The synthesis method using phosphorus trichloride and acetic acid as raw materials has low raw material price and relatively simple operation, and has become the main method for industrially producing hydroxyethylidene diphosphonic acid at present. French patent Fr1521963, under the condition of 35°C, after adding phosphorus trichloride to acetic acid and aqueous solution, gradually raise the temperature, collect the by-product acetyl chloride, and drop the collected acetyl chloride back into the reaction system. In this method, the dropwise addition of phosphorus trichloride must be controlled at a lower temperature, the reaction time is long, and the energy consumption is large. Chinese patent CN1091137 improves the cooling system in the method of Fr1521963, and adds the collected by-product acetyl chloride to the acetic acid solution, reducing the consumption of raw material acetic acid. However, the reaction time is long and the energy consumption is large. U.S. Patent No. 3,366,676 proposes adding phosphorus trichloride to acetic acid and tributylamine, and the reaction mixture is heated to 136° C. in a closed container. Although the reaction is complete in a short time, the presence of amine affects the purity of the product. Belgian patent Belg.672168 adds phosphorus trichloride to acetic acid at room temperature, then slowly raises the temperature to 60°C, then rises to 110°C, separates the acetylated intermediate product, and hydrolyzes to obtain the product. This method needs to separate the acetylated product, which complicates the operation process.

发明内容Contents of the invention

本发明的目的在于提出一种改进的羟基乙叉二膦酸生产方法,以缩短反应时间,降低能耗,提高反应的安全性。The purpose of the present invention is to propose an improved production method of hydroxyethylidene diphosphonic acid, to shorten the reaction time, reduce energy consumption and improve the safety of the reaction.

本发明提出的羟基乙叉二膦酸的改进生产方法,是将醋酸直接与三氯化磷反应,得到乙酰化的羟基乙叉二膦酸,然后水解生成羟基乙叉二膦酸溶液。具体步骤是将醋酸置于反应釜底,升温至100℃-120℃。开动搅拌,滴加三氯化磷,同时开通冷凝器,分离和回收乙酰氯和氯化氢,乙酰化的羟基乙叉二膦酸迅速产生。随着乙酰化的羟基乙叉二膦酸生成,反应液逐渐变粘稠。三氯化磷加完之后,保温1~3小时,然后通蒸汽水解,即得到羟基乙叉二膦酸溶液,同时回收醋酸溶液。The improved production method of hydroxyethylidene diphosphonic acid proposed by the present invention is to directly react acetic acid with phosphorus trichloride to obtain acetylated hydroxyethylidene diphosphonic acid, and then hydrolyze to generate hydroxyethylidene diphosphonic acid solution. The specific steps are to place the acetic acid at the bottom of the reaction kettle and raise the temperature to 100°C-120°C. Stirring is started, phosphorus trichloride is added dropwise, and the condenser is opened at the same time to separate and recover acetyl chloride and hydrogen chloride, and acetylated hydroxyethylidene diphosphonic acid is produced rapidly. With the generation of acetylated hydroxyethylidene diphosphonic acid, the reaction solution gradually becomes viscous. After the phosphorus trichloride is added, keep it warm for 1-3 hours, and then pass steam for hydrolysis to obtain the hydroxyethylidene diphosphonic acid solution, and recover the acetic acid solution at the same time.

本发明的路线是将反应原料醋酸与三氯化磷直接反应,反应温度应在100℃以上,优选的反应温度为110℃以上。在此温度下,三氯化磷和醋酸迅速生成乙酰化的羟基乙叉二膦酸,并释放出乙酰氯和盐酸。反应式如下:The route of the present invention is to directly react the raw material acetic acid and phosphorus trichloride, and the reaction temperature should be above 100°C, preferably above 110°C. At this temperature, phosphorus trichloride and acetic acid rapidly generate acetylated hydroxyethylidene diphosphonic acid, and release acetyl chloride and hydrochloric acid. The reaction formula is as follows:

本发明中,醋酸与三氯化磷的摩尔比为3.5∶1~8∶1。醋酸与三氯化磷的摩尔比较大时,产生的乙酰化的羟基乙叉二膦酸与醋酸明显分层,可以进行分离,分离出乙酰化的羟基乙叉二膦酸,进行水解得到羟基乙叉二膦酸。分离出的醋酸,合并入反应原料继续循环使用。该过程也可以不进行分离,也就是说分离过程不是必须的。In the present invention, the molar ratio of acetic acid to phosphorus trichloride is 3.5:1-8:1. When the molar ratio of acetic acid to phosphorus trichloride is large, the resulting acetylated hydroxyethylidene diphosphonic acid and acetic acid are obviously layered and can be separated, and the acetylated hydroxyethylidene diphosphonic acid is separated and hydrolyzed to obtain hydroxyethylidene diphosphonic acid. bisphosphonic acid. The separated acetic acid is merged into the reaction raw materials and continues to be recycled. This process can also be without separation, that is to say, the separation process is not necessary.

所选用的原料醋酸,浓度大于98%,最好为99%以上,也可以将回收的醋酸溶液吸收反应过程中回收的乙酰氯后循环使用。通过此步骤,可以降低原料消耗。The selected raw material acetic acid has a concentration greater than 98%, preferably more than 99%. The recovered acetic acid solution can also be recycled after absorbing the recovered acetyl chloride in the reaction process. Through this step, raw material consumption can be reduced.

实施本发明,反应可以迅速进行,大大缩短反应时间,降低能耗,节约成本;由于反应釜中水的含量极少或几乎无水,增加了三氯化磷滴加过程的安全性;反应过程不需要将收集的乙酰氯返滴回反应釜中,可以全部用作本发明的原料。By implementing the present invention, the reaction can be carried out quickly, greatly shortening the reaction time, reducing energy consumption, and saving costs; because the content of water in the reactor is very little or almost anhydrous, the safety of the phosphorus trichloride dropping process is increased; the reaction process The collected acetyl chloride does not need to be dripped back into the reactor, and all of it can be used as the raw material of the present invention.

具体实施方式Detailed ways

下面通过实例进一步描述本发明。The present invention is further described below by way of example.

实例1 将90克醋酸加入到反应釜底,开动搅拌器,加热升温至100℃,滴加68克三氯化磷,同时开通冷凝器,并收集乙酰氯和盐酸。半小时后,加完三氯化磷,继续升温至115℃,保温1小时,通蒸汽水解,得到90克含量47%的羟基乙叉二膦酸溶液。其中亚磷酸含量0.5%。Example 1 Add 90 grams of acetic acid to the bottom of the reaction kettle, start the agitator, heat up to 100°C, add 68 grams of phosphorus trichloride dropwise, and simultaneously open the condenser to collect acetyl chloride and hydrochloric acid. Half an hour later, after adding phosphorus trichloride, continue to heat up to 115° C., keep warm for 1 hour, pass steam for hydrolysis, and obtain 90 grams of hydroxyethylidene diphosphonic acid solution with a content of 47%. Wherein the content of phosphorous acid is 0.5%.

实例2 将120克醋酸加入到反应釜底,开动搅拌器,加热升温至110℃,滴加68克三氯化磷,同时开通冷凝器,并收集乙酰氯和盐酸。25分钟后,加完三氯化磷,继续升温至115℃,保温1.5小时,通蒸汽水解,得到102克含量46%的羟基乙叉二膦酸溶液。其中亚磷酸含量0.3%。Example 2 Add 120 grams of acetic acid to the bottom of the reaction kettle, start the agitator, heat up to 110°C, add 68 grams of phosphorus trichloride dropwise, and simultaneously open the condenser to collect acetyl chloride and hydrochloric acid. After 25 minutes, after adding phosphorus trichloride, continue to heat up to 115° C., keep warm for 1.5 hours, and conduct steam hydrolysis to obtain 102 grams of 46% hydroxyethylidene diphosphonic acid solution. Wherein the content of phosphorous acid is 0.3%.

实例3 将180克醋酸加入到反应釜底,开动搅拌器,加热升温至105℃,滴加68克三氯化磷,同时开通冷凝器,并收集乙酰氯和盐酸。30分钟后,加完三氯化磷,继续升温至115℃,保温2小时,通蒸汽水解,得到90克含量48%的羟基乙叉二膦酸溶液。其中亚磷酸含量0.2%。Example 3 Add 180 grams of acetic acid to the bottom of the reaction kettle, start the agitator, heat up to 105°C, add 68 grams of phosphorus trichloride dropwise, and simultaneously open the condenser to collect acetyl chloride and hydrochloric acid. After 30 minutes, after adding phosphorus trichloride, continue to heat up to 115° C., keep warm for 2 hours, pass steam for hydrolysis, and obtain 90 grams of hydroxyethylidene diphosphonic acid solution with a content of 48%. Wherein the content of phosphorous acid is 0.2%.

实例4 将150克98%醋酸加入到反应釜底,开动搅拌器,加热升温至100℃,滴加68克三氯化磷,同时开通冷凝器,并收集乙酰氯和盐酸。25分钟后,加完三氯化磷,继续升温至115℃,保温1小时,通蒸汽水解,得到86克含量50%的羟基乙叉二膦酸溶液。其中亚磷酸含量0.2%。Example 4 150 grams of 98% acetic acid was added to the bottom of the reaction kettle, the stirrer was started, the temperature was raised to 100°C, 68 grams of phosphorus trichloride was added dropwise, and the condenser was opened simultaneously to collect acetyl chloride and hydrochloric acid. After 25 minutes, after adding phosphorus trichloride, continue to heat up to 115° C., keep warm for 1 hour, pass steam for hydrolysis, and obtain 86 grams of 50% hydroxyethylidene diphosphonic acid solution. Wherein the content of phosphorous acid is 0.2%.

实例5 将120克99%醋酸加入到反应釜底,开动搅拌器,加热升温至105℃,滴加68克三氯化磷,同时开通冷凝器,并收集乙酰氯和盐酸。20分钟后,加完三氯化磷,继续升温至115℃,保温2小时,通蒸汽水解,得到88克含量49%的羟基乙叉二膦酸溶液。其中亚磷酸含量0.3%。Example 5 120 grams of 99% acetic acid was added to the bottom of the reaction kettle, the stirrer was started, the temperature was raised to 105°C, 68 grams of phosphorus trichloride was added dropwise, and the condenser was opened simultaneously to collect acetyl chloride and hydrochloric acid. After 20 minutes, after adding phosphorus trichloride, continue to heat up to 115° C., keep warm for 2 hours, pass steam for hydrolysis, and obtain 88 grams of hydroxyethylidene diphosphonic acid solution with a content of 49%. Wherein the content of phosphorous acid is 0.3%.

Claims (4)

1. An improved production method of hydroxyethylidene diphosphonic acid is characterized in that acetic acid is placed at the bottom of a reaction kettle, the temperature is raised to 100-120 ℃, phosphorus trichloride is dripped under stirring, a condenser isopened simultaneously, acetyl chloride and hydrogen chloride are separated and recovered, and acetylated hydroxyethylidene diphosphonic acid is rapidly generated; then steam is introduced for hydrolysis to obtain hydroxyethylidene diphosphonic acid solution, and simultaneously, the acetic acid solution is recovered.
2. The production process as set forth in claim 1, wherein the molar ratio of acetic acid to phosphorus trichloride is 3.5: 1 to 8: 1.
3. The process according to claim 1, wherein the concentration of acetic acid is greater than 98%.
4. The process according to claim 1, wherein the acetyl chloride recovered in the reaction is absorbed in the recovered acetic acid solution and recycled.
CN 02137110 2002-09-24 2002-09-24 Method for producing 1-hydroxy ethylene-1,1-diphosphonic acid Pending CN1418883A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1312163C (en) * 2005-05-11 2007-04-25 江苏江海化工有限公司 Hydroxy ethylidene diphosphonic acid with content of greater than or equal to 90 percent and process for making same
CN100348603C (en) * 2006-03-29 2007-11-14 傅明珠 Process for synthesis of hydroxy ethidene diphosphoric acid
WO2011023280A1 (en) * 2009-08-28 2011-03-03 Synthon B.V. Process for making 1-hydroxyalkylidene-1,1-biphosphonic acids
CN103265576A (en) * 2013-05-22 2013-08-28 山东省泰和水处理有限公司 Low-concentration acetic acid concentrating process for hydroxyl ethylidene diphosphonic acid production process
CN106046048A (en) * 2016-05-31 2016-10-26 常州姚氏同德化工有限公司 Method for preparing etidronic acid with high raw material utilization rate
CN106083924A (en) * 2016-05-31 2016-11-09 常州姚氏同德化工有限公司 A kind of preparation method of 1-hydroxy ethylidene-1,1-diphosphonic acid

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1312163C (en) * 2005-05-11 2007-04-25 江苏江海化工有限公司 Hydroxy ethylidene diphosphonic acid with content of greater than or equal to 90 percent and process for making same
CN100348603C (en) * 2006-03-29 2007-11-14 傅明珠 Process for synthesis of hydroxy ethidene diphosphoric acid
WO2011023280A1 (en) * 2009-08-28 2011-03-03 Synthon B.V. Process for making 1-hydroxyalkylidene-1,1-biphosphonic acids
CN103265576A (en) * 2013-05-22 2013-08-28 山东省泰和水处理有限公司 Low-concentration acetic acid concentrating process for hydroxyl ethylidene diphosphonic acid production process
CN106046048A (en) * 2016-05-31 2016-10-26 常州姚氏同德化工有限公司 Method for preparing etidronic acid with high raw material utilization rate
CN106083924A (en) * 2016-05-31 2016-11-09 常州姚氏同德化工有限公司 A kind of preparation method of 1-hydroxy ethylidene-1,1-diphosphonic acid

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