APPARATUS AND METHOD FOR CONTINUOUS PRODUCTION OF POLYETHYLENE GLYCOL DINITRATE

Abstract

An apparatus for producing polyethylene glycol dinitrate. The apparatus includes providing continuously an acid composition and a glycol composition to a reaction apparatus; reacting the acid composition and the glycol composition in the reaction apparatus in a continuous manner to generate a reaction composition; using an alkaline composition to at least partially neutralize the reaction composition to cause at least a portion of the polyethylene glycol dinitrate to deposit from a solution of the reaction composition; and extracting the deposit of polyethylene glycol dinitrate.

Claims

1-13. (canceled)

14. A reaction apparatus for producing in a continuous manner polyethylene glycol dinitrate (PEGDN), characterized in that the reaction apparatus includes a series of reaction cells spatially disposed in one or more planar structures, the plurality of reaction cells constitute; a feed preparation section having feedstreams for continuously providing an acid composition and a glycol composition to reaction cells thereof, wherein the acid composition includes a mixture of dilute nitric acid and concentrated sulphuric acid; a nitration section in which the acid composition and the glycol composition react in reaction cells in a continuous manner to generate a reaction composition; a quench and neutralization section having a feed for a cooling arrangement for cooling reaction cells to avoid spatial reaction hotspots and thereby preventing thermal runaway occurring within the reaction apparatus, and a plurality of feeds for providing an alkaline composition to at least partially neutralize the reaction composition to cause at least a portion of the polyethylene glycol dinitrate to deposit from a solution of the reaction composition; and a separation arrangement for extracting the deposit of polyethylene glycol dinitrate.

15. The reaction apparatus of claim 14, characterized in that the dilute nitric acid has a concentration in a range of 50-70 weight %.

16. The reaction apparatus of claim 15, characterized in that the dilute nitric acid has a concentration of 60 weight %.

17. The reaction apparatus of claim 14, characterized in that the nitric acid is at a concentration in a range of 96-98 weight %.

18. The reaction apparatus of claim 14, characterized in that the glycol composition includes PEG in a range of PEG150-PEG800.

19. The reaction apparatus of claim 14, characterized in that the alkaline composition includes Ammonium Hydroxide which is added in sufficient quantity to the reaction composition so as to neutralize the reaction composition.

20. The reaction apparatus of claim 19, characterized in that the reaction composition, when neutralized has a pH in a range of 4 to 12.

21. The reaction apparatus of claim 14, characterized in that the separation arrangement is operable to separate the PEGDN and Ammonium Nitrate using a hydrophobic solvent.

22. The reaction apparatus of claim 21, characterized in that the hydrophobic solvent is one of methylene chloride, a hexane, a pentane or a silicone.

23. The reaction apparatus of claim 14, characterized in that the feed for the cooling arrangement uses a coolant applied to a region which is spatially adjacent to the series of reaction cells.

24. The reaction apparatus of claim 21, characterized in that the series of reaction cells are cooled in operation using a coolant at a temperature in a range of 0 C. to 15 C.

Description

DESCRIPTION OF THE DIAGRAMS

[0032] Embodiments of the present disclosure will now be described, by way of example only, with reference to the following diagrams wherein:

[0033] FIG. 1 is an illustration of an apparatus for producing PEGDN and ammonium nitrate, according to an embodiment of the present disclosure;

[0034] FIG. 2 is an illustration of an apparatus for producing PEGDN and ammonium nitrate, according to another embodiment of the present disclosure; and

[0035] FIG. 3 is an illustration of steps of a method for producing PEGDN and ammonium nitrate, according to an embodiment of the present disclosure.

[0036] In the accompanying diagrams, an underlined number is employed to represent an item over which the underlined number is positioned or an item to which the underlined number is adjacent. A non-underlined number relates to an item identified by a line linking the non-underlined number to the item. When a number is non-underlined and accompanied by an associated arrow, the non-underlined number is used to identify a general item at which the arrow is pointing.

DESCRIPTION OF EMBODIMENTS OF THE DISCLOSURE

[0037] The present disclosure generally relates to an apparatus and a method for continuous production of polyethylene glycol dinitrate (PEGDN). Specifically, the apparatus of present disclosure provides improved manufacturing of PEGDN. The PEGDN may be used in conjunction with combustible hydrocarbon fuels. Generally, such apparatus and method employ a process which is based on the below mentioned reactions:

[Aliphatic polyol]+[HNO.sub.3].fwdarw.Nitrate esters Eq. 1

[Aliphatic polyol]+[HNO.sub.3]+[H.sub.2SO.sub.4].fwdarw.Nitrate esters Eq. 2

[0038] However, the present disclosure is primarily concerned with an improved apparatus and method of producing PEGDN. The improved method employs a process which is based on the below mentioned reactions:

PEG+[HNO.sub.3].fwdarw.PEGDN+ammonium nitrate Eq. 3

PEG+[HNO.sub.3]+[H.sub.2SO.sub.4].fwdarw.PEGDN+ammonium nitrate Eq. 4

[0039] Referring now to FIG. 1, shown is an apparatus 100 for producing Dinitrate (PEGDN), according to an embodiment of the present disclosure. The apparatus 100 uses nitric acid and PEG for the production of PEGDN. Specifically, the apparatus 100 is configured to mix and react the chosen reagents, to subsequently generate an aqueous stream treated with an alkali, and, finally separate reaction products (PEGDN or another nitrate ester) from the aqueous stream.

[0040] As shown, the apparatus 100 includes a feedstream 102 for introducing a substrate aliphatic polyol, specifically PEG. The apparatus 100 also includes another feedstream 104 for introducing nitric acid. The apparatus 100 further includes a plurality of reaction cells such as reaction cells 106a, 106b, 106c, 106d, 106e and 106f having planer structure. The feedstreams 102, 104 along with the reaction cells 106a, 106b constitute a feed preparation section of the apparatus 100. Further, as shown, the reaction cells 106c, 106d constitute a nitration section, and the reaction cells 106e, 106f constitute a quench and neutralization section of the apparatus 100. The quench and neutralization section of the apparatus 100 includes a feed 108 for a cooling arrangement, and a plurality of feeds 110a, 110b and 110c for Ammonium hydroxide or ammonia to quench and neutralise a reaction composition (i.e. PEG together with nitric acid). The apparatus 100 also includes a separation arrangement 112 in which a biphasic product containing PEGDN and aqueous ammonium nitrate is separated.

[0041] Referring now to FIG. 2, shown is an apparatus 200 for producing PEGDN, according to another embodiment of the present disclosure. The apparatus 200 of FIG. 2 is substantially structurally and functionally similar to the apparatus 100 of FIG. 1, however, the apparatus 200 includes a provision for another feedstream 202. Specifically, a feed preparation section of the apparatus 200 includes the feedstream 202 for introducing sulphuric acid over and above the feedstream 104 (of the apparatus 100).

[0042] The apparatus of FIGS. 1 and 2 are susceptible to being used for manufacturing other types of fuel additives, if required, for example other types of nitrate esters.

[0043] Referring now to FIG. 3, illustration of steps of a method 300 of continuously producing PEGDN is shown, in accordance with an embodiment of the present disclosure. Specifically, the method 300 relates to the apparatuses of FIGS. 1 and 2 for the production of PEGDN.

[0044] Step 302, continuously provides an acid composition and a glycol composition to a reaction apparatus.

[0045] Step 304, the acid composition and the glycol composition react in the reaction apparatus in a continuous manner to generate a reaction composition.

[0046] Step 306, an alkaline composition is used to at least partially neutralize the reaction composition and to cause at least a portion of the polyethylene glycol dinitrate to deposit from a solution of the reaction composition.

[0047] Step 308, the deposit of polyethylene glycol dinitrate is extracted.

[0048] The steps 302 to 308 are only illustrative and other alternatives can also be provided where one or more steps are added, one or more steps are removed, or one or more steps are provided in a different sequence without departing from the scope of the claims herein. For example, the method 300 also includes separating the PEGDN and Ammonium Nitrate using a hydrophobic solvent. The method 300 is further explained in detail in conjunction with few examples.

EXAMPLE 1

Synthesis and Purification of PEGDN

Example 1.1

Synthesis of PEGDN using Continuous Flow and Concentrated Nitric Acid

[0049] Example 1.1 mainly corresponds to FIG. 1, in which the preparation of the nitrate ester PEGDN is performed in an advanced flow reactor (such as the apparatus 100). The 100 ml of strong nitric acid (80-99 weight % or 96-98 weight %) and 100 ml of glycol are mixed. The reaction mixture is cooled with refrigerated heat transfer fluid like ethylene glycol, applied spatially adjacent to the series of reaction cells to maintain the specified reaction temperature (0-15 C.). The series of reaction cells, spatially disposed in one or more planar structures in which the acid composition and the glycol composition mix in a turbulent manner determine the purity of the product. The reaction cells are cooled in operation to avoid spatial reaction hotspots and thereby prevent thermal runaway occurring within the reaction apparatus. The neutralization of the acidic reactant composition includes introduction of sufficient Ammonium Hydroxide to effect neutralisation of the reaction mixture. The neutralised mixture has a pH in the range of 4-12. The two phase liquid product is then fed into a continuous separation arrangement for receiving the reaction composition and separating therefrom in a continuous manner polyethylene glycol dinitrate (PEGDN) and ammonium nitrate solution. In the separating arrangement the hydrophobic solvent used for extracting the PEGDN is one of methylene chloride and similar polyhalogenated hydrocarbons, a pentane or a hexane. The reagents were bought from Fisher Scientific, and had at least 99% degree of purity.

Example 1.2

Synthesis of PEGDN using Continuous Flow and Nitric Acid and Concentrated Sulphuric acid

[0050] Example 1.2 corresponds to FIG. 2, i.e. the preparation of the PEGDN uses 50 ml of strong sulphuric acid (i.e., 80-99 weight % or 96-98 weight %) and dilute nitric acid (i.e. 50-70 weight % or 60 weight %) instead of only using the strong nitric acid. Also, the preparation of the PEGDN includes use of 50 ml of pure PEG. It may be evident to those skilled in the art that the preparation Example 1.2 follows the same subsequent steps as explained in Example 1.1.

EXAMPLE 2

Retrieval of Ammonium Nitrate

[0051] Example 2 corresponds to both FIGS. 1 and 2, i.e. the PEGDN separates out of solution during the addition of the ammonium hydroxide as the pH is approaching neutrality. The two phase liquid product is then fed into a continuous separation arrangement and the PEGDN thus is recovered using a hydrophobic solvent which is one of methylene chloride and similar polyhalogenated hydrocarbons, a hexane, a pentane or a silicone. After phase separation two products are obtained. The first is the required product, PEGDN. The second is a solution of ammonium nitrate, which is a well known fertiliser.

[0052] Further, the aforementioned PEGDN and similar additives can be added to fuels, for example alcohols, heavy fuel oil, LNG, PNG and similar. Such alcohols include, for example: ethanol, methanol.

[0053] Modifications to embodiments of the disclosure described in the foregoing are possible without departing from the scope of the disclosure as defined by the accompanying claims. Expressions such as including, comprising, incorporating, consisting of, have, is used to describe and claim the present disclosure are intended to be construed in a non-exclusive manner, namely allowing for items, components or elements not explicitly described also to be present. Reference to the singular is also to be construed to relate to the plural. Numerals included within parentheses in the accompanying claims are intended to assist understanding of the claims and should not be construed in any way to limit subject matter claimed by these claims.