Patent Application
20190001239
The present invention relates to a composition containing an anionic surfactant based on an alkali salt of sulfosuccinic acid dialkylester to promote the obtention of an inverse microemulsion which is used as foam control composition in a phosphoric acid production medium. The present invention also discloses a process to produce said composition by stirring the components of such a composition to obtain a microemulsion. The invention also aims at a method for controlling foam during the production of phosphoric acid by wet process, avoiding its formation or decreasing its amount.
Phosphoric acid is produced by two general routes.
In the first process called “thermal process” the raw material is the elemental phosphorous. However, this process is highly energy consuming, thus it has been abandoned in favor of the second process called “wet” route which is more economic.
The typical “wet” process for preparing phosphoric acid comprises the decomposition of phosphate rock with sulfuric acid. Tricalcium phosphate that is present in the phosphate rock is converted by reaction with concentrated sulphuric acid into phosphoric acid and insoluble calcium sulphate salt (gypsum).
Then, water is added and the insoluble calcium sulphate is removed, most usually by filtration, along with other insoluble impurities.
Side reactions also take place simultaneously due the presence of calcium fluoride and calcium carbonate in the phosphate rock.
The side reactions involved in the wet process of phosphoric acid release large volumes of carbon dioxide, and some hydrogen fluoride gas, resulting in the development of substantial amounts of foam. Besides that, soil organic components commonly present in phosphate rocks act as interfacial agent, giving stability to the bubbles formed. Those soil organic components are known under the name Kerogen, which is a mixture of several organic components naturally present in rocks. The quantity of those soil organic components varies from 0.01% by weight and 1% by weight in the rock, depending on the source. The higher the amount of kerogen in the rock, the higher the severity of the foam.
The foam produced is critical to a safe and cost effective operation since the foam reduces the maximum volume and/or capacity of the vessel used and consequently decreases the maximum throughput and the overall productivity of the total chain process. Additionally, the process may result in overflows of foam which can lead to hazardous conditions for plant personnel due to the corrosive properties of phosphoric acid and this may create also large quantities of incompletely reacted materials foaming into the vapor condensing systems or waste disposal system, causing costly repairs and yield losses.
Several antifoams agents have been proposed to control foam generated in such process, including oil based agents, water based agents, powder defoamers, like silicone based, EO/PO based and polymers based defoamers.
The U.S. Pat. No. 4,083,936 discloses the use of certain phosphate esters of aliphatic alcohols as defoaming agents. This phosphate ester is dispersed in water and 2.5% of one emulsifier, like di-2-ethylhexylsulfosuccinate, is added to form an emulsion. However, the emulsion described in this document is not an inverse microemulsion but a regular emulsion. Indeed, they are using a low surfactant concentration and a high water concentration, thus the system is based on a dispersion of the oil phase in water. In other words, the continuous phase is water, and this fact does not allow the “delivery” effect of the emulsion on the reactor surface, as it will be dispersed in the whole reactor, decreasing the effectiveness of the defoamer at the top part of the vessel. Furthermore, this emulsion has only 2.5% of emulsifier, which cannot form a microemulsion, resulting in a thermodynamically unstable emulsion and consequently a phase separation over time.
In the U.S. Pat. No. 4,415,472, it is proposed to use a mixture of alkali salts of succinic acid dialkylesters and higher aliphatic alcohols as defoaming agent for phosphate decomposition media. In this case, there is no production of an inverse microemulsion with oxygenated solvent in the internal phase, and therefore it is not possible to achieve an efficient and oriented effect in the foam concentrated on the reactor surface. As explained before, without the specific structure, the oxygenated solvent is not delivered efficiently, remaining dispersed in the reaction medium, and therewith the foam is not rapidly eliminated.
One of the objects of the invention is to propose an improved composition system acting as a defoamer, breaking down the foam already formed and decreasing its volume or quantity on the reactor surface.
A further object of the invention is to propose an improved composition acting as an antifoaming avoiding the foam to be formed during the process for producing phosphoric acid by decomposition of phosphate rock with sulfuric acid.
Another objective of the present invention is to propose a translucent and thermodynamically stable microemulsion, with no phase separation before reaching the point of action.
The invention thus proposes a foam control composition for phosphoric acid production, by wet process, comprising at least one anionic surfactant based on an alkali salt of sulfosuccinic acid dialkylester, at least one C8-C28 fatty acid ester, at least one C8-C28 fatty acid and at least one oxygenated solvent.
The present invention also provides a process to produce the foam control composition by adding the fatty acid ester, the fatty acid and the alkali salt of sulfosuccinic acid dialkylester, in this specific order, stirring until complete homogenization, adding the oxygenated solvent and stirring, preferably until obtaining a microemulsion.
Also, the present invention proposes a method for controlling foam during a process for producing phosphoric acid by decomposition of phosphate rock with sulfuric acid, comprising the addition of the foam control composition. The method for controlling foam can be a method for decreasing the amount of foam or a method for avoiding the formation of foam.
Then, another object of the present invention is a process for producing phosphoric acid comprising the addition of the foam control composition, at any position of the production vessel, more preferably at the top over the reaction medium. This addition can be applied before, together or after the phosphate rock, during the decomposition step, at any position inside of a reactor vessel.
The expression “inverse microemulsion” in the sense of the present invention is a dispersion made of a polar compound phase comprising at least one oxygenated solvent, an oily phase comprising at least one fatty acid ester and at least one fatty acid, and a surfactant being at least the anionic surfactant based on an alkali salt of sulfosuccinic acid dialkylester, wherein the dispersed phase is the polar compound phase comprising at least one oxygenated solvent and the continuous phase is the oily phase comprising at least one fatty acid ester and at least one fatty acid. Each time “microemulsion” term is used, it is preferably an inverse microemulsion.
A “fatty” according to the invention is a chain of an even number of carbon atoms chosen from 8 to 28 included.
By “at least one C8-C28 fatty acid ester”, it is understood that C8-C28 refers to the fatty acid part of the fatty acid ester.
The present invention provides a foam control composition to control the foam during the production of phosphoric acid by decomposition of phosphate rock with sulfuric acid. The foam control composition for phosphoric acid production according to the invention contains a mixture of at least one anionic surfactant based on an alkali salt of sulfosuccinic acid dialkylester, at least one C8-C28 linear or branched fatty acid ester, at least one C8-C28 linear or branched fatty acid and at least one oxygenated solvent.
In a preferred embodiment, the foam control composition according to the invention is in the form of a microemulsion, more preferably in the form of inverse microemulsion, wherein the oxygenated solvent, which acts as solubilizing agent of organic compounds foam stabilizers, is protected inside the aggregates (dispersed phase). Furthermore, the fatty acid ester present in the continuous phase promotes the delivery of the microemulsion on the reactor surface and it also acts as foam destabilizing.
Throughout this specification, the anionic surfactant acts to promote spreading of the oxygenated solvent and may also have other functions in this composition, as aggregate maker, maintaining the oxygenated solvent dispersed into the oily phase, giving the “delivery” property.
Examples of compounds falling into the scope of this term are anionic surfactants based on an alkali salt of sulfosuccinic acid dialkylester. Preferably, the alkyl groups of the dialkyl ester are similar or different and are selected from the group consisting of C6-C12 linear or branched alkyl groups and mixtures thereof. They are preferably selected from the group consisting of C6-C10 branched alkyl groups and mixtures thereof; more preferably a C8 branched alkyl group; and even more preferably 2-ethylhexyl. In a preferably embodiment the alkali salt of sulfosuccinic acid dialkylester is selected from sodium or potassium salt of sulfosuccinic acid dialkylesters and mixtures thereof, and it is more preferably selected from sodium salt of sulfosuccinic acid dialkylesters. Even more preferably the alkali salt of sulfosuccinic acid dialkylester is bis (2-ethylhexyl) sodium sulfosuccinate, also commercially available under the name DHAYSULF 70B® by SOLVAY.
In one embodiment, the foam control composition comprises the alkali salt of sulfosuccinic acid dialkylester in an amount of about 10% to 60%, preferably about 20% to 50% by weight based on the total weight of the foam control composition.
In a favorable embodiment the foam control composition according to the present invention comprises bis (2-ethylhexyl) sodium sulfosuccinate in an amount of 25% to 40% by weight based on the total weight of the foam control composition.
The fatty acid ester according to the invention is advantageously selected from the group consisting of C8-C28 linear or branched fatty acid esters. It is preferably selected from the group consisting of fatty acid esters having C8-C28 saturated or unsaturated aliphatic chains on the fatty acid part of the ester, and mixtures thereof. It is more preferably selected from the group consisting of C16-C18 saturated or unsaturated aliphatic chains on the fatty acid part of the ester. In a preferable embodiment the alcohol part of the fatty acid ester is selected from the group consisting of C2-C8 linear or branched alkyl groups, and it is more preferably selected from C3-C6 linear or branched alkyl groups. Even more preferably the fatty acid ester is isobutyl oleate, also commercially available under the name DHAYTAN IS® by SOLVAY.
One preferred embodiment is when the foam control composition according to the present invention comprises the fatty acid ester in an amount of about 20% to 60%, preferably about 30% to 50% by weight based on the total weight of the foam control composition.
The fatty acid according to the invention is selected from the group consisting of C8-C28 linear or branched fatty acids. It is preferably selected from the group consisting of C16-C18 saturated or unsaturated aliphatic fatty acids. More preferably the fatty acid is soybean fatty acid, also commercially available under the name SOFA® by JIUJIANG LISHAN ENTECH Co.
In a favorable embodiment the foam control composition according to the present invention comprises the fatty acid in an amount of about 2% to 30%, preferably about 10% to 20% by weight based on the total weight of the foam control composition.
The oxygenated solvent is selected from the group consisting of aliphatic dibasic acid esters, glycerol ketals or acetals, polyalkylene glycols and mixtures thereof. It is preferably a mixture of aliphatic dibasic acid esters, and even more preferably a mixture comprising dimethyl glutarate, dimethyl succinate and dimethyl adipate, also commercially available under the name RHODIASOLV® RPDE by SOLVAY. In another embodiment the oxygenated solvent is a glycerol ketal or acetal, more preferably 2,2-dimethyl-4-hydroxymethyl-1,3-dioxolane, also commercially available under the name AUGEO® SL191 by SOLVAY.
In another embodiment the foam control composition according to the present invention comprises the oxygenated solvent in an amount of about 2% to 30%, preferably about 10% to 20% by weight based on the total weight of the foam control agent composition.
In a particular embodiment of the present invention, the foam control composition consists in a mixture of an anionic surfactant based on an alkali salt of sulfosuccinic acid dialkylester, a C8-C28 linear or branched fatty acid ester, a C8-C28 linear or branched fatty acid and an oxygenated solvent.
In another embodiment the foam control composition according to the present invention comprises bis (2-ethylhexyl) sodium sulfosuccinate, isobutyl oleate, soybean fatty acid and a mixture comprising dimethyl glutarate, dimethyl succinate and dimethyl adipate. Preferably the foam control composition according to the present invention comprises 25 to 40% by weight of bis (2-ethylhexyl) sodium sulfosuccinate, 30 to 50% by weight of isobutyl oleate, 10 to 20% by weight of soybean fatty acid and 10 to 20% by weight of a mixture comprising dimethyl glutarate, dimethyl succinate and dimethyl adipate.
In another embodiment the foam control composition according to the present invention comprises bis (2-ethylhexyl) sodium sulfosuccinate, isobutyl oleate, soybean fatty acid and 2,2-dimethyl-4-hydroxymethyl-1,3-dioxolane. Preferably the foam control composition according to the present invention comprises 25 to 40% by weight of bis (2-ethylhexyl) sodium sulfosuccinate, 30 to 50% by weight of isobutyl oleate, 10 to 20% by weight of soybean fatty acid and 10 to 20% by weight of 2,2-dimethyl-4-hydroxymethyl-1,3-dioxolane.
The invention also provides a process for producing the foam control composition as described above. The process comprises the following steps:
In a particular embodiment of the present invention, the fatty acid ester, the fatty acid and the alkali salt of sulfosuccinic acid dialkylester are added with a 5-30 minutes, preferably about 15 minutes interval between each addition.
According to the invention, the fatty acid can be added in the reactor at a temperature from 40° C. to 90° C.
In the step (b), the solution obtained at step (a) is advantageously stirred at a temperature of from 10° C. to 90° C. preferably from 20° C. to 40° C. and at a stirring speed of from 40 rpm to 250 rpm.
Then, according to step (c), the oxygenated solvent is added in the solution obtained at step (b) and the solution obtained at step (c) is advantageously stirred at a stirring speed of from 40 rpm to 250 rpm, during about 30 minutes, preferably until a microemulsion is obtained.
The method for controlling foam during a process for producing phosphoric acid by decomposition of phosphate rock with sulfuric acid comprises the addition of the foam control composition, at any position of the production vessel, more preferably at the top over the reaction medium. This addition can be applied before, together or after the phosphate rock is added in the reactor.
When the foam control composition is added before or together with the phosphate rock, throughout or inside of the reaction medium, the action is to prevent the foam formation formation due its presence near to the site reaction, thus the composition act as an antifoaming agent.
Adding the foam control composition after the reaction between the sulfuric acid and the phosphate rock, in other words, when the addition of the composition is in a top down fashion towards the foam, this composition acts mainly as a defoamer agent, disrupting and decreasing the foam already present at the top of the vessel.
Without being limited to theory, it is believed that in both cases, as the composition has a low density, it is directed to the reactor surface, where is the foam generated during the process for producing phosphoric acid. In this environment, the microemulsion system is disrupted, releasing the oxygenated solvent, which decreases the foam stability. This action is caused by its solubilizing effects on organic compounds present in the reaction medium, which are responsible for foam stability.
Moreover, the anionic surfactant acts as spreading agent for the fatty acid and fatty acid ester, as they are hydrophobic immiscible agents when they collided with the air bubbles of the foam they modified the surface shape of these bubbles, favoring the coalescence between them and thus breaking the water film.
The process for producing phosphoric acid by decomposition of phosphate rock with sulfuric acid is well known by the skilled person in the art. The phosphoric acid is produced from fluorapatite, known as phosphate rock, by the addition of concentrated sulfuric acid, as described in the following general steps:
In the first step, the phosphate rock is decomposed by the action of concentrated sulfuric acid and this reaction is advantageously performed at a temperature of about from 40° C. to 100° C. preferably from 45° C. to 85° C.
The addition of the foam control composition to the reaction medium of step (a) can be applied before, together or after the addition of the phosphate rock is added in the reactor, at any position inside of the reactor vessel.
In the step (b), the solution obtained at step (a) can be separated by filtration to obtain the phosphoric acid.
Then, according to step (c), the phosphoric acid is purified for example by solvent extraction using, for example, methyl isobutyl ketone (MIBK) in which the acid is slightly soluble and concentrated to give 60% P2O5 content.
Other details or advantages of the invention will become more clearly apparent in the light of the examples given below.
For the examples below, the parameters have been measured according to the foam height, i.e., the lowest the height of the foam provides the highest efficiency of the foam control composition.
The evaluation of foam control performance was verified by the defoaming tests described below.
To implement the first defoaming test, 195 g of phosphoric acid (with 27% P2O5) were placed in a one-liter graduate cylinder and heated up to 75° C. To this heated acid were added 15 mL of 37% hydrochloric acid.
40 μL of a foam control composition comprising 28% by weight of bis (2-ethylhexyl) sodium sulfosuccinate, 30 to 50% by weight of isobutyl oleate, 10 to 20% by weight of soybean fatty acid and 10 to 20% by weight of a mixture comprising dimethyl glutarate, dimethyl succinate and dimethyl adipate was added to this mixture of blend acids and an agitator rotating at 250 rpm was used to stir and after that 15 g of ore (rock) were added.
No foam control composition was added to this mixture of blend acids. 15 g of ore (rock) were added under stirring rotating at 250 rpm.
For Example 1 and Comparative example 1, the ore contains 0.8 to 1% of kerogen (high amount of kerogen).
The foaming heights were measured at given time intervals during 60 seconds and compared.
The effectiveness of the tested foam control compositions are shown in the table I below.
The above results show that the foam control composition described in this invention disrupts more quickly the foam generated in the process, having lower foam height during the first seconds and, in addition, prevent the foam generation, keeping the lowest foam level over time.
To implement the second defoaming test, 195 g of phosphoric acid (with 25% P2O5) were placed in a 500 mL graduate cylinder and heated up to 75° C. To this heated acid were added 15 mL of 37% hydrochloric acid.
50 ppm of a foam control composition comprising 28% by weight of bis (2-ethylhexyl) sodium sulfosuccinate, 30 to 50% by weight of isobutyl oleate, 10 to 20% by weight of soybean fatty acid and 10 to 20% by weight of a mixture comprising dimethyl glutarate, dimethyl succinate and dimethyl adipate was added to this mixture of blend acids and an agitator rotating at 250 rpm was used to stir and after that 15 g of ore (rock) were added.
The following comparative compositions 2a, 2b and 2c were added to the mixture of blend acids, in the same amount (50 ppm) and an agitator rotating at 250 rpm was used to stir and after that, 15 g of ore (rock) were added.
The dosage of foam control composition is described as ppm of total amount of phosphorous source (phosphoric acid+ore(rock)). In this example, we are putting 15 g ore+195 g phosphoric acid=210 g. So, 50 ppm of 210 g=0.0105 g=about 10 microliters of foam control additive.
For Example 2 and Comparative examples 2a, 2b and 2c, the ore contains 0.02 to 0.05% of kerogen (lower amount of kerogen compared to part 1).
The foaming heights were measured at given time intervals during 60 seconds and compared.
The effectiveness of the tested foam control compositions are shown in the table II below.
The above results show that the foam control composition described in this invention disrupts more quickly the foam generated in the process, having lower foam height during the first seconds and, in addition, prevent the foam generation, keeping the lowest foam level over time.
| Number | Date | Country | Kind |
|---|---|---|---|
| 15176074.1 | Jul 2015 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IB2016/000961 | 7/5/2016 | WO | 00 |
