MXPA97007350A - Hydrocarbon microencapsulated process - Google Patents
Hydrocarbon microencapsulated processInfo
- Publication number
- MXPA97007350A MXPA97007350A MXPA/A/1997/007350A MX9707350A MXPA97007350A MX PA97007350 A MXPA97007350 A MX PA97007350A MX 9707350 A MX9707350 A MX 9707350A MX PA97007350 A MXPA97007350 A MX PA97007350A
- Authority
- MX
- Mexico
- Prior art keywords
- petrochem
- pounds
- hydrocarbon
- kilograms
- hydrocarbons
- Prior art date
Links
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 47
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 21
- 239000000126 substance Substances 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 13
- 238000009472 formulation Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000002253 acid Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N silicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 3
- 229910052814 silicon oxide Inorganic materials 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- KUXGUCNZFCVULO-UHFFFAOYSA-N 2-(4-nonylphenoxy)ethanol Chemical compound CCCCCCCCCC1=CC=C(OCCO)C=C1 KUXGUCNZFCVULO-UHFFFAOYSA-N 0.000 claims description 2
- 239000004115 Sodium Silicate Substances 0.000 claims description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N Sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 230000001804 emulsifying Effects 0.000 claims description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 2
- 229920000847 nonoxynol Polymers 0.000 claims description 2
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 2
- 241000894007 species Species 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims description 2
- LIVNPJMFVYWSIS-UHFFFAOYSA-N Silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 claims 1
- 230000002378 acidificating Effects 0.000 claims 1
- 238000011109 contamination Methods 0.000 abstract 1
- 235000012239 silicon dioxide Nutrition 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 239000004698 Polyethylene (PE) Substances 0.000 description 1
- 235000008452 baby food Nutrition 0.000 description 1
- 229910052729 chemical element Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drugs Drugs 0.000 description 1
- 235000020673 eicosapentaenoic acid Nutrition 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 239000001963 growth media Substances 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
Abstract
This invention relates to two chemical products and the process of applying them to hydrocarbon residues contaminated with hydrocarbons that results in the microencapsulation of contaminating hydrocarbon residues in a silicon dioxide microcell, thus avoiding the direct contact of these hydrocarbons with the environment. and therefore the pollution of the ecological environment. The object of this invention is to provide an efficient and definitive solution to the problems of contamination of the environment by hydrocarbon residues. The A.B.E. PETROCHEM has the characteristic of breaking the surface tension of hydrocarbons and permanently trapping them. The S.S. PETROCHEM reacts instantly with the A.B.E. PETROCHEM being trapped the hydrocarbon in the cell that is formed by the reaction between these two chemicals. The application process is a fundamental part for the microencapsulation to be really effective. This means that their control as described was a necessary characteristic to achieve optimal results. Likewise, the realization of the aforementioned analyzes, let us know the real progress of the process
Description
"HYDROCARBON MICROENCAPSULATED PROCESS"? BACKGROUND OF THE INVENTION This invention arises from the current needs of coating with a reliable, efficient and effective ecological technology that helps to prevent and solve the problems of pollution due to hydrocarbon residues. Silicates have been widely used over time in many different ways including ecological, but without giving the desired results. So based on this, the formulation of A.B.E. PETROCHEM and S.S. PETROCHEM Emulsifiers, like silicates, have been widely used in many fields of the /. industry, so the important thing was to develop a specific formula to break the surface tension of hydrocarbons and also react with a silicate, in order to definitively isolate the polluting residues of hydrocarbons. In this way the formulas of A.B.E. PETROCHEM and S.S. PETROCHEM. Of great importance is also the application process of these chemical products since without the technique described in DESCRIPTION OF THE INVENTION it is not possible to achieve the results of microeacapsular in definitive form to the hydrocarbon residues. On February 20, 1997, the Mexican Institute of Industrial Property was requested through
* _ of the Department of Searches, Documentary Fund and Microfilm a national and international technical search regarding the hydrocarbon microencapsulation process. This search resulted
tecaüzación of 20 references, but none is related to the characterizations of the process of microencapsulation- hydrocarbons, nor with the characterizations of the formulation of A.B.E.
PETROCHEM and S.S. PETROCHEM
DESCRIPTION OF THE INVENTION The hydrocarbon microencapsulation process is a chemical treatment that turns hazardous hydrocarbon residues or contaminated with hydrocarbons into non-hazardous and reusable; It is an ecological technology. There are other similar technologies that have not given the results obtained with the hydrocarbon mkroencapsulation process, mainly due to large differences in the formulation of the chemical products used and their application process. The invention consists of: The formulation of two chemical products as well as the process of applying them to hydrocarbon residues or soils contaminated with hydrocarbons, regardless of the type of hydrocarbon, for the purpose of confining hydrocarbon residues in an oxide microcell. of silicon, pure, amorphous, inert, impermeable and insuppressible, formed by the instant chemical reaction of ABE PETROCHEM and dd S.S. PETROCHEM and the correct application of these through the process described here. This microcell avoids all contact of the polluting elements with the environment.
FORMULATION AND PREPARATION OF THE CHEMICAL PRODUCTS A.B.E. PETROCHEM The formulation dd A.B.E. PETROCHEM is characterized by the following components: 1. Methanol 2% 9.90 pounds 2. Glycol Ether 3% 14.85 pounds 3. WITCO SN-70 4% 19.80 pounds 4. Nonyl Phenol Ethoxylate (N-95) 8% 39.60 pounds 5. DOBSA 3% 14.85 pounds 6. Water 12% 59.40 pounds 7. Phosphoric Acid (75%) 10% 49.50 pounds 8. Murine Acid 20 degrees Bauroé (HCL) 28% 138.60 pounds Shake 30 to 45 minutes. 9. Water 30% 148.50 pounds
Pack in polyethylene drums. Weight per drum 495 lbs.
H.H. PETROCHEM The formulation of the S.S. PETROCHEM is characterized by the following components: 1. Sodium Silicate Solution (40-41 Baumé) 90% 562.50 pounds, "Note: Silicate solutions can vary in density.The pounds per drum can vary from 595 to 625. 2 Water 10% 62.50 pounds
Shake for 30 minutes or complete the solution between products. 15 Pack in metal drums. Weight per drum from 595 to 625 pounds.
APPLICATION PROCESS. The hydrocarbon microencapsulation process is carried out with a ribbon mixer. The batten mixers are designed to mix with great efficiency and for this they are used in the preparation of medicines and in the preparation of baby food. The material to be treated (waste contaminated with any type of hydrocarbons or hydrocarbon residues) is weighed. In a 173-ft1 mixer of capacity it can be processed from 1, 000 to 1,500 kilograms depending on the characteristics of the material. Then let us add 1,000 or 1,500 kilograms of material to the mixer. Step 1. The material is homogenized for 5 minutes, a sample is taken to run a retort analysis, and pH is also measured.
The retort analysis results in a percentage of hydrocarbons in the sample and consists of distilling the hydrocarbons and water present. Step 2. Once known d percentage of hydrocarbons and pH, the chemical products A.B.E. are dosed. PETROCHEM and the S.S. PETROCHEM. As an example of dosage, we can mention the following: If the percentage of hydrocarbons is between 35 and 40, the dosage of A.B.E. PETROCHEM should be 5 gallons per thousand kilograms, and the dosage of S.S. PETROCHEM should also be 5 gallons per thousand kilograms because the molar ratio between A.B.E. PETROCHEM and the S.S. PETROCHEM is one on one. The aforementioned dosage was found to be optimal by means of the trial and error method and consequent analysis of the results. If d% - * ^ of hydrocarbons is between 41 and 50 the dosage dd A.B.E. PETROCHEM should be 8 gallons per thousand kilograms and k) both the dosage of S.S. PETROCHEM will also be 8 gallons per thousand kilograms. Step 3. The first chemical that is applied is A.B.E. PETROCHEM, and is done by spraying with an electric pump with HP% engine and at an expense of 3 gallons per minute The A.B.E.
PETROCHEM has the characteristic of emulsifying any chemical species of hydrocarbon, that is to say, it acts in all d range of BHL (Hydrophilic Lipophilic Balance) so when contacting the hydrocarbon it emulsifies it and traps it permanently surrounding it at a microscopic level. Step 4. After 15 or 20 minutes of mixing, measure pH d which should be in d acid range, if not, add more A.B.E. PETROCHEM until obtaining the acid value. 20 Step 5. Once in the acid range, proceed to apply S.S. PETROCHEM also for asperete and with an electric pump with HP V * engine and at an expense of 3 gallons per minute. The S.S. PETROCHEM reacts instantly with the A.B.E. PETROCHEM that previously trapped the polluting hydrocarbon, and it is at the moment of this reaction that the microcell of silicon oxide is formed. 25 Step 6. After 15 minutes of mixing, measure the pH d which should be in the range of 7.0 to
8. 5, u d value is in that range d material is treated and ready to be unloaded from the ribbon mixer. If this is not the case, more S.S. PETROCHEM, with mixing, until the pH value is in d foran or indicated. It is important to mention that d total volume at the end of treatment, only increases from 10 to one
% maximum, this is: 5 1,000 kilograms of material to be treated will become, by the addition of chemical products, 1,010 kilograms or 1,020 kilograms of non-hazardous material susceptible to be rendered useless without damage to the environment. Step 7. Once the treated material is discharged, it is placed in a sampling area. ** ^ Step 8. In its opportunity, the following is analyzed: a) Water in oil by the EPA OIL IN WATER method. b) CRETTB in accordance with the Official Mexican Standards. This ensures that the treated material is no longer a hazardous waste. c) Edaphic analyzes that verify the content of chemical elements and physical characteristics adequate to make the treated material a culture medium. We attach to this document copies of CRETIB analysis certificates made in accordance with the
Official Mexican Standards for samples of hazardous hydrocarbon residues treated by the hydrocarbon microencapsulation process. We also attach a copy of the opinion issued by the Laboratory of
Edafocli atología of the Center for Biological Research of the Autonomous University of the State of
Mordos in order to demonstrate the effectiveness of the process. Therefore, it can be stated that the characteristics of this hydrocarbon microencapsulation process together with the formulation of the mentioned chemical products have not been achieved by any other similar technology.
Claims (3)
- A.B.E. PETROCHEM and S.S. PETROCHEM, taking into account the "dosage guide: Dd 5 to 25% 3 gallons of both productß per thousand kilograms. From 26 to 34% 4 gallons of both products per thousand kilograms. 0 Dd 35 to 40% 5 gallons of both products per thousand kilograms. From 41 to 50% 8 gallons of both products per thousand kilograms. Dd 51 to 55% 11 gallons of both products per thousand kilograms. This dosing table was found to be optimal by the trial and error method and analysis of the results. 5 Step 3. The first chemical that is applied is A.B.E. PETROCHEM, and is made by spraying with an electric pump with motor (HP V and at an expense of 3 gallons per minute) A.B.E.
- PETROCHEM has the characteristic of emulsifying any hydrocarbon chemical species, it is dedr, it acts in all d range of BHL (Hydrophilic Lipophilic Balance) so when it contacts the hydrocarbon it emulsifies it and traps it permanently surrounding it at the microscopic level. Step 4. After 15 or 20 minutes of mixing, measure pH d which should be in the acidic range, 5 if not, add more A.B.E. PETROCHEM until obtaining the acid value. Step 5. Once in the acid range, proceed to apply S.S. PETROCHEM also by sprinkling and with similar equipment. The S.S. PETROCHEM reacts instantly with the A.B.E. PETROCHEM that previously trapped the polluting hydrocarbon, and it is at the moment of this reaction that the microcell of silicon oxide is formed. - "* Step 6. After 15 minutes of mixing it is measured d pH d which should be in d range of 7.0 a 8. 5, if d is in that range the material is treated and ready to be discharged from the batten mixer. If this is not the case, more S.S. PETROCHEM, with mixing, until the pH value is in the specified range. It is important to mention that d total volume at the end of the treatment, only increases from 10 to 15 20% maximum, this is: 1,000 kilograms of material to be treated will become, by the addition of chemical products, 1,010 kilograms or 1,020 kilograms of non-hazardous material that can be rendered useless without damage to the environment. 20 2. The formulation of A.B.E. PETROCHEM. The formulation of A.B.E. PETROCHEM is characterized by the following components: 1. Methanol 2% 9.90 pounds 2. Glycol Ether 3% 14.85 pounds 3. WITCO SN-70 4% 19.80 pounds 25 4. Nonyl Phenol Ethoxylate (N-9S) 8% 39.60 Works 5. D0BSA 3% 14.85 pounds 6. Water 12% 59.40 pounds 7. Phosphoric Acid (75%) 10% 49.50 pounds 8. Murine Acid 20 degrees Baumé (HCL) 28% 138.60 pounds Shake 30 to 45 minutes. 9. Water 30% 148.50 pounds
- 3. The formulation of S.S. PETROCHEM The formulation of the S.S. PETROCHEM is characterized by the following components: 1. Sodium Silicate Solution (40-41 Baumé) 90% 562.50 lbs. Note: Silicate solutions may vary in density. The pounds per drum can vary from 595 to 625. 2. Water 10% 62.50 pounds Shake for 30 minutes or until the solution is completed between products.
Publications (1)
Publication Number | Publication Date |
---|---|
MXPA97007350A true MXPA97007350A (en) | 1999-04-27 |
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