Method for reducing foam in a primary fractionator

Abstract

The present invention includes methods for improving the operational parameters in primary fractionators which are experiencing diminished operation efficiencies due to deposits of polymerized hydrocarbon species. The invention comprises the step of adding a foam reducing amount of a foam reducing composition at the primary fractionator. A reduction in foaming is achieved whereby the operational efficiency of the process is improved based upon operation parameters including, but not limited to, liquid-gas contact ratio, product top temperature, pressure differentials, gasoline end point or combinations thereof.

Description

BACKGROUND AND SUMMARY OF THE INVENTION

[0001] This invention relates to a method of operating a primary fractionator, also termed a quench tower, in an ethylene plant with anti-foulants, particularly defoamers.

[0002] In the manufacture of lighter hydrocarbon products such as ethylene, heavier hydrocarbons such as naphtha or diesel oil are cracked in pyrolysis heaters at temperatures of approximately 850° C. to form mixtures of smaller molecules including, but not limited to, ethylene, propylene, and butadiene. Such mixtures, commonly termed cracked gases, are cooled in various stages of an ethylene plant until they are separated in the fractionation section of the ethylene plant

[0003] During primary heat recovery, the cracked gases pass through and are cooled by a series of heat exchangers, also termed transfer line exchangers, before being quenched with a heavy oil. This heavy oil, which is known as quench oil or bottoms quench oil, accumulates in the bottom of the primary fractionator. The primary fractionator contains varying components of fuel oil species ranging from the bottoms of the column to the beginning of what is called the rectification section of the column. The rectification section of the column is prone to severe fouling problems related to species such as styrene, indene, di-vinyl benzene, alpha-methyl styrene, indene derivatives, naphthalene and other higher ring compound derivatives.

[0004] The polymerization products of these species deposit at a very rapid rate not only on upper tray surfaces, but also beneath tray surfaces. Due to this fouling problem, an increase in column pressure drop along with reduction in fractionation efficiencies are experienced. Consequently, the quality of gasoline condensing in the quench water tower and also the quality of fuel oil made from the system are negatively effected. Typically, the problem of fouling in the rectification section is also accompanied by poor viscosity control in the bottom of the quench oil tower due to improper operations of the primary fractionator. The deposition of the fouling species, commonly as polymers, obstructs the vapor and liquid flow inside the fractionator and due to the reduced surface area available, the environment is conducive to increased froth/foam generation in the column. The presence of foam further increases the pressure drop and results in entrainment of higher boiling point products into the lighter products and vice versa. Due to excessive foaming, the column pressure drop increases very rapidly and is a major reason for reduced unit efficiencies.

[0005] As fouling continues to occur, the rate of foaming also increases in the column resulting in plant operators having to reduce unit feed rates significantly and, ultimately, shut down the plant for cleaning the primary fractionator.

[0006] The present invention provides a method to operate primary fractionators which are fouled due to polymer deposition by providing an appropriate chemical agent to extend run-length of the primary fractionator.

BRIEF DESCRIPTION OF THE DRAWINGS

[0007] FIG. 1 illustrates data for Example 1 in which the feed rate, reflux rate, and column pressure of a primary fractionation column are plotted against time.

[0008] FIG. 2 illustrates data for Example 2 collected at in which column pressure for a quench tower is plotted against time.

DETAILED DESCRIPTION OF THE INVENTION

[0009] The present invention includes methods for reducing foam in primary fractionators which are experiencing diminished operation efficiencies due to deposits of polymerized hydrocarbon species. The invention comprises the step of adding a foam reducing amount of a foam reducing composition at the primary fractionator. A reduction in foaming is achieved whereby the operational efficiency of the process is improved based upon operation parameters including, but not limited to, liquid-gas contact ratio, product top temperature, pressure differentials, gasoline end point or combinations thereof.

[0010] The preferred foam reducing composition is a polysiloxane. A representative polysiloxane useful in the present invention is dimethyl polysiloxane. This is a commercially available chemical which can be purchased, for example, from Dorf Ketal Chemicals India Pvt. Ltd. Other suitable foam reducing compositions include, but are not limited to, ethylene oxide-propylene oxide copolymers, fatty acid ethoxylates, poly-iso-butylenes and fatty acid esters. Suitable examples of these compounds are also available from Dorf Ketal Chemicals India Pvt. Ltd.

[0011] The foam reducing composition may be added to the process in neat form, or in any suitable solvent. Representative solvents may be aromatic in character and include, but are not limited to, toluene, xylene, naphtha. It is preferred that the foam reducing composition be applied either upstream of the particular site experiencing foaming problems or directly to the site of the foaming problem. Specifically, the deposit reducing composition may be added continuously or periodically to the primary fractionator reflux. Primary fractionators may themselves include internal components including ripple trays, sieve trays, bubble cap trays, valve trays

[0012] The preferred polysiloxane described above may be applied to the process at end use concentrations ranging from 0.0001% to 0.1% with 0.0005% to 0.0025% being the preferred range (all percentages herein are expressed on a weight/weight basis). These percentages convert into working dosage rates of 1 part per million to about 1000 parts per million hydrocarbon. Specific dosages may be determined by the conditions existing in the particular process. Although the most preferred range for a polysiloxane is provided, it is understood that the present invention is not to be limited by the specific compound or concentration set forth herein. It is further envisioned that the present invention may be applied to the process along with other hydrocarbon treatment agents such as corrosion inhibiting compositions.

[0013] The following examples are provided in order to more clearly illustrate the present invention, and while being illustrative, are in no way meant to be construed as limiting the scope of the present invention.

EXAMPLE 1

[0014] An ethylene production plant utilizing naphtha in the production of light hydrocarbons including ethylene, propylene, and butadiene experienced fouling of the primary fractionator resulting in reduction of column efficiencies even when operated at lower than normal feed rates. Considering the loss of column efficiencies indicated by higher column pressure drop and increased gasoline end point even at 20% reduced plant feed rates, the plant operators contemplated shutting the unit down to clean the column.

[0015] However, the present invention was practiced on the respective process in order to achieve acceptable operational parameters and the utility of the present invention was thusly demonstrated. An anti-foaming agent comprising a polysiloxane was injected along with the reflux to the column. The particular agent was dimethyl polysiloxane available from Dorf Ketal Chemicals India Pvt. Ltd. and was fed into the column so as to achieve a working concentration of approximately 100 parts per million.

[0016] Within a few hours of using the anti-foaming agent, column pressure drop was reduced as shown in FIG. 1. It was observed that during the fouled condition, the gasoline end point had increased by 20° C., which was also reflected in the color of the respective gasoline. The fouled condition resulted in a brownish colored gasoline in contrast to gasoline normally having a yellowish green coloration. After the polysiloxane compound was injected into the reflux, the plant operators subsequently observed that the color of the gasoline was restored to its normal yellowish green color, along with reduction in gasoline end point indicating improvement of the column operations.

[0017] FIG. 1 illustrates the data associated with this experiment wherein time is provided on the X axis and the kilograms per hour of feed rate and reflux mass are provided on the left hand Y axis. In addition, pressure drop in kilograms per centimeter2 is provided on the right hand Y axis. Arrow A indicates the initial injection of the polysiloxane compound into the reflux. Column pressure was measured, as indicated on the X axis. A dramatic reduction in column pressure is evident from the data presented in graphic form.

EXAMPLE 2

[0018] A plant experienced fouling problems due to increased column pressure drop. The pressure drop in this plant operated at normal values of 0.07 to 0.08 kilograms per centimeter2. However, the fouling problems resulted in much elevated values ranging from 0.135 to 0.15 kilograms per centimeter2. With the fouling problem, reduced feed rates and reflux rates were observed although the pressure drop in the column remained high.

[0019] In order to avoid a costly shut down of the manufacturing facility, the plant operators utilized the present invention wherein polysiloxane was injected into the quench oil tower at an injection rate of 10 to 20 parts per million based on column reflux rates. The specific polysiloxane utilized was identical to that of Example 1.

[0020] Within hours after the initial injection of the anti-foam, operators observed column pressure reduced to a value of approximately 0.109 kilograms per centimeter2 while the column feed rates improved from 175 tons per hour of naphtha to 184 tons per hour of naphtha. During the same time period, reflux rates increased from 20 tons per hour to 30 tons per hour. The improvement in column operations are shown in FIG. 2 in which sampling times are indicated along the X axis and column pressures are indicated in kilograms per centimeter2 on the Y axis.

[0021] While the invention has been described with reference to preferred embodiments, those skilled in the art will appreciate that certain substitutions, alterations and omissions may be made without departing from the spirit of the invention. Accordingly, the foregoing description is meant to be exemplary only and should not limit the scope of the invention set forth in the following claims.

Claims

1. A method for reducing pressure drop in an operating fouled or non-fouled primary fractionator used for fractionation and primary heat recovery in a cracked gas producing plant, comprising the steps of: a) directing cracked gas into the primary fractionator for removal of heat from the cracked gas wherein the cracked gas exits through an overhead of the primary fractionator; and b) adding an anti-foulant to the primary fractionator whereby pressure drop is reduced in the operating primary fractionator.

2. A method according to claim 1 wherein the anti-foulant includes at least one antifoaming agent.

3. A method according to claim 2 wherein the anti-foaming agent is selected from the group consisting of a polysiloxane, an ethylene oxide-propylene oxide copolymer, a fatty acid ethoxylate, a poly-iso-butylene and a fatty acid ester.

4. A method for normalizing a temperature profile in an operating fouled or non-fouled primary fractionator used for fractionation and primary heat recovery in a cracked gas producing plant, comprising the steps of: a) directing cracked gas into the primary fractionator for removal of heat from the cracked gas wherein the cracked gas exits through an overhead of the primary fractionator; and b) adding an anti-foulant to the primary fractionator whereby the temperature profile in the operating primary fractionator is normalized.

5. A method according to claim 4 wherein the anti-foulant includes at least an anti-foaming agent.

6. A method according to claim 5 wherein the anti-foaming agent is selected from the group consisting of polysiloxane, an ethylene oxide-propylene oxide copolymer, a fatty acid ethoxylate, a poly-iso-butylene and a fatty acid ester.

7. A method for improving fractionation in an operating fouled or non-fouled primary fractionator used for fractionation and primary heat recovery in a cracked gas producing plant, comprising the steps of: a) directing cracked gas into the primary fractionator for removal of heat from the cracked gas wherein the cracked gas exits through an overhead of the primary fractionator; and b) adding an anti-foulant to the primary fractionator whereby fractionation is improved during subsequent operation of the operating primary fractionator.

8. A method according to claim 7 wherein the anti-foulant includes at least an anti-foaming agent.

9. A method according to claim 8 wherein the anti-foaming agent is selected from the group consisting of polysiloxane, an ethylene oxide-propylene oxide copolymer, a fatty acid ethoxylate, a poly-iso-butylene and a fatty acid ester.

10. A method for reducing foam in a primary fractionator used in a hydrocarbon manufacturing process, comprising the steps of: a) introducing a foam reducing amount of a foam reducing composition into the primary fractionator; and b) operating the hydrocarbon manufacturing process so that the foam is reduced whereby at least one operational parameter of said process is improved.

11. A method according to claim 10 wherein the foam reducing composition includes at least a polysiloxane, an ethylene oxide-propylene oxide copolymer, a fatty acid ethoxylate, a poly-isobutylene and a fatty acid ester.

12. A method according to claim 10 wherein the operation efficiency of the hydrocarbon manufacturing process is based on at least one of liquid-gas contact ratio, feed rate, reflux rate, and product top temperature, gasoline end point or pressure differential.

13. A method according to claim 10 wherein the foam reducing composition is a polysiloxane provided in the foam reducing amount of greater than about 0.01 parts per million.

14. The method of claim 10 wherein the foam reducing amount of the foam reducing composition is introduced into the quench tower to achieve a dosage in the range of about 0.01 parts per million to about 5000 parts per million.

15. A method according to claim 10 further comprised by the step of: c) measuring an operation efficiency of the fractionator based on at least one of liquid-gas contact ratio, feed rate, reflux rate, product top temperature, gasoline end point or pressure differential.

16. A method according to claim 10 wherein the foam reducing composition is introduced into the primary fractionator in a reflux flow.

17. A method according to claim 16 wherein the foam reducing composition is continuously introduced into the primary fractionator in a reflux flow.

18. A method according to claim 16 wherein the foam reducing composition is periodically introduced into the primary fractionator in a reflux flow.

19. A method according to claim 10 wherein the foam reducing composition further includes a solvent selected from the group consisting of toluene, xylene and naphtha.

20. A method according to claim 10 wherein the polysiloxane is dimethyl polysiloxane.