United States Patent (19) 11 Patent Number: 4,865,129 Ryles 45 Date of Patent: Sep

Total Page:16

File Type:pdf, Size:1020Kb

United States Patent (19) 11 Patent Number: 4,865,129 Ryles 45 Date of Patent: Sep United States Patent (19) 11 Patent Number: 4,865,129 Ryles 45 Date of Patent: Sep. 12, 1989 (54) HIGH TEMPERATURE PROFILE Attorney, Agent, or Firm-Frank M. Van Riet MODIFICATION AGENTS AND METHODS 57 ABSTRACT FOR USING SAME A new and improved composition and method for pro 75) Inventor: Roderick G. Ryles, Milford, Conn. file modification of subterranean formations character 73) Assignee: American Cyanamid Company, ized by high reservoir temperatures and/or harsh brine conditions are disclosed. The new and improved profile Stamford, Conn. modification agents comprise a gelable composition (21) Appl. No.: 226,713 comprising: (22 Filed: Aug. 1, 1988 (a) water; (b) a water-thickening and crosslinkable amount of a water-dispersible copolymer comprising from Related U.S. Application Data about 1 to about 99 mol % of units derived from an 62 Division of Ser. No. 946,265, Dec. 24, 1986, Pat. No. N,N-dialkylacrylamide monomer copolymerized 4,788,228. with from about 1 to about 99 mol % of units de 51 Int. Cl." .......................... E21B33/138; E21B 43; rived from acrylic acid or a salt thereof; and E21B 20 (c) an amount of a polyvalent metal sufficient to 52 U.S.C. .................................... 166/295; 166/274; crosslink the copolymer to form a stable gel. The 252/8.551; 252/8.554; 523/130 profile modification agents are effective to alter the 58 Field of Search ....... 252/8.551 APS, 8.554 APS; permeability of preselected portions of an under 523/130; 166/274, 295 ground formation by forming strong gels which are stable in harsh brine attemperatures of up to about 56 References Cited 120° C. The composition and method are particu U.S. PATENT DOCUMENTS larly adapted for use in enhanced oil recovery operations. 3,502,149 3/1970 Pence, Jr. .................... ... 166/295 3,727,689 4/1973 Clampitt. 252/8.551 Additionally, component (b) can be a water-dispersible 3,762,476 10/1973 Gall ................. ... 166/273 X terpolymer comprising from about 5 to about 75 mol 3,785,437 1/1974 Clampitt et al. ... ... 166/295 X percent of units derived fron an N,N-dialkylacryla 3,981,363 9/1976 Gall ..................................... 166/270 mide, from about 5 to about 35 mol percent of units 4,563,290 1/1986 Okada et al. 252/8.554 derived from acrylic acid or salts thereof and from 4,669,920 6/1987 Dymond .......................... 252/8.551 about 10 to about 90 mol percent of units derived from 4,799,548 1/1989 Mumallah et al. ............. 166/295 X 2-acrylamido-2-methylpropanesulfonic acid or salts 4,814,096 3/1989 Evani ............................... 252/8.554 thereof. Primary Examiner-John F. Terapane Assistant Examiner-Gary Geist 13 Claims, No Drawings 4,865,129 1. 2 zones. The mobility of a fluid in a permeable geological HIGH TEMPERATURE PROF LE formation is the effective permeability of the formation MODIFICATION AGENTS AND METHODS FOR to that fluid divided by the viscosity of the fluid. In the USING SAME past, a conventional method for reducing the mobility of drive fluids through permeable formations has been This is a division of application, Ser. No. 06/946,265, to increase the drive fluids viscosity. Such an increase in filed Dec. 24, 1986 now U.S. Pat. No. 4,788,228. viscosity is generally accomplished by using viscous solutions of high molecular weight polymers such as BACKGROUND OF THE INVENTION polyacrylamides, cellulose ethers, polysaccarides and The present invention relates to profile modification 10 the like. Such polymeric solutions have been found agents for altering the permeability of preselected por effective for reducing the water:oil ratio in the total tions of a subterranean formation. In preferred embodi producing well effluent and for increasing the daily ments, the present invention relates to a new and im production of hydrocarbonaceous fluids. proved composition and method for profile modifica In actual field practice, however, such mobility alter tion of a subterranean hydrocarbon-containing forma 5 ing polymers elute out of producing wells quickly and tion to reduce water:oil ratios and improved petroleum the water:oil ratios rapidly rise back to an undesirable recovery during enhanced oil recovery operations. level necessitating retreatment of the producing interval More particularly, it relates to new and improved aque with the viscous polymer solutions. These viscosity ous gelable compositions exhibiting high temperature increasing polymers are relatively expensive materials gel stability at temperatures up to about 150 C. and in 20 and a one time treatment would be particularly desir harsh brines and methods for using same. able. The enhanced secondary recovery of oil from oil More recently, reduction in the permeability of the bearing or containing subterranean formations by fluid pre-selected portions of various subterranean oil bear drive processes, wherein a fluid is injected into the ing formations has been accomplished with gelable formation by one or more injection wells to drive the oil 25 solutions of polymeric materials. The formation of gels through the formation to one or more production wells by the cross-linking of polymers is well known in the art is a known process, commonly referred to as enhanced for this purpose. A great deal of literature has been oil recovery. Fluids used in such processes include liq generated concerning the formation of gels in situ in uids such as water and various hydrocarbons, and gases underground formations for the purpose of treating the such as hydrocarbon gases, carbon dioxide, steam, etc. 30 formations to better produce oil and gas from bore holes Many oil reservoirs comprise layers or zones of porous drilled into the formations and to decrease undesired rock which can vary in permeability from zone to zone. water output. It is well recognized that polymer gels In all fluid drive processes, a recognized problem is the and processes incorporating same facilitate the plugging predilection of the drive fluid to channel along or of underground formations in desired areas e.g. by mod through the more permeable zones of the formation. 35 ifying the fluid flow profile, and in particular by de This is commonly referred to as channeling. Another creasing the relative permeability of the most permeable problem is viscous fingering which occurs, for example, portions of the formations. by the over-ride of a viscous fluid by a less viscous fluid. Prior art gelling compostions for use in profile modi The more conductive zones after the oil has been fication applications generally comprise water, poly largely displaced therefrom function as "thief zones' 40 mers capable of being cross-linked by polyvalent metal which permit the drive fluid to channel directly from cations and polyvalent metalion crosslinker. Prior art injection to production wells. In many instances, such crosslinkable polymers have included polyacrylamides, channeling or fingering results in leaving substantial carboxymethylcelluloses and polysaccharides, gener quantities of oil in the less permeable zones of the for ally of high molecular weight in excess of one million. mation which are bypassed. Such channeling or finger 45 A commonly used system for generating polyvalent ing can occur when the mobility i.e. the quotient of the metal ions has been to provide them in the form of reservoir's permeability to the drive fluid divided by the chelated metal ion complexes or as part of a redox sys viscosity of the drive fluid becomes large relative to the tem. The redox system will generally comprise redox mobility of the reservoir oil. couples wherein oxidizing agent is selected from water One of the significant problems, therefore, attendant 50 soluble compounds of polyvalent metals wherein the to the production of oil and gas from subterranean hy metal is present in a valence state which is capable of drocarbon containing formations, is the concomitant being reduced to a lower polyvalent state as exemplified production of water. Such produced water can be reser by potassium permanganate, sodium permanganate, voir water occasioned by coning or a similar phenom ammonium chromate, ammonium dichromate, the alkali ena of the aquifier, or it can be injection water from 55 metal chromates, the alkali metal dichromates and chro secondary or tertiary recovery treatments being applied mium trioxide. Sodium dichromate and potassium di to the formation. Whatever the source, there is an upper chromate because of low cost and ready availability are limit beyond which water production can no longer be the most widely used of the oxidizing agents. The re tolerated and its further entry into the producing well ducing agents in the redox couples have included sulfur bore must at least be reduced if further production of 60 containing compounds such as sodium or potassium hydrocarbon resources at that location is to be contin sulfide, sodium or potassium hydrosulfide, sodium or ued. potassium metabisulfite, sodium or potassium bisulfite, Regardless of whether the undesired water is a natu hydrogen sulfide, sodium or potassium thiosulfate, thi ral drive fluid or an artificial drive fluid such as from oacetamide and others, as well as non-sulfur containing secondary or tertiary recovery projects, the problem is 65 compounds, such as hydroquinone, perahydrazinoben primarily occasioned by the predilection of the drive zoic acid, hydrazine phosphite, hydrazine dichloride fluid to preferentially seek the higher permeability and others. Illustrative prior art profile modification zones and to more or less bypass the lower permeability compositions and methods are disclosed in U.S. Pat. 4,865,129 3 4. Nos. 2,718,497; 3,502,149; 3,727,689; 3,749,172; In commonly assigned copending application, Ser. 3,762,476; 3,785,437; 3,795,276; 3,952,806; 3,964,923; No. 729,512, now U.S. Pat. No. 4,746,687 there is dis 3,981,363; 4,018,286; 4,039,029; 4,040,484; 4,043,921; closed copolymers of 1) 2-acrylamido-2-methylpro 4,055,502; 4,110,230; 4,120,361; and 4,498,539 to list but a few.
Recommended publications
  • Crown Chemical Resistance Chart
    Crown Polymers, Corp. 11111 Kiley Drive Huntley, IL. 60142 USA www.crownpolymers.com 847-659-0300 phone 847-659-0310 facisimile 888-732-1270 toll free Chemical Resistance Chart Crown Polymers Floor and Secondary Containment Systems Products: CrownShield covers the following five (4) formulas: CrownShield 50, Product No. 320 CrownCote, Product No. 401 CrownShield 40-2, Product No. 323 CrownShield 28, Product No. 322 CrownPro AcidShield, Product No. 350 CrownCote AcidShield, Product No. 430 CrownPro SolventShield, Product No. 351 CrownCote SolventShield, Product No. 440 This chart shows chemical resistance of Crown Polymers foundational floor and secondary containment product line that would be exposed to chemical spill or immersion conditions. The chart was designed to provide general product information. For specific applications, contact your local Crown Polymers Floor and Secondary Containment Representative or call direct to the factory. ; Resistant to chemical immersion up to 7 days followed by wash down with water 6 Spillage environments that will be cleaned up within 72 hours after initial exposure. 9 Not Recommended Chemical CrownShield SolventShield AcidShield Chemical CrownShield SolventShield AcidShield 1, 4-Dichloro-2-butene 9 6 6 Aluminum Bromate ; ; ; 1, 4-Dioxane 9 6 6 Aluminum Bromide ; ; ; 1-1-1 Trichloroethane 9 ; ; Aluminum Chloride ; ; ; 2, 4-Pentanedione 6 ; 6 Aluminum Fluoride (25%) ; ; ; 3, 4-Dichloro-1-butene 6 6 6 Aluminum Hydroxide ; ; ; 4-Picoline (0-50%) 9 6 6 Aluminum Iodine ; ; ; Acetic Acid (0-15%) 9 6 6
    [Show full text]
  • Gasket Chemical Services Guide
    Gasket Chemical Services Guide Revision: GSG-100 6490 Rev.(AA) • The information contained herein is general in nature and recommendations are valid only for Victaulic compounds. • Gasket compatibility is dependent upon a number of factors. Suitability for a particular application must be determined by a competent individual familiar with system-specific conditions. • Victaulic offers no warranties, expressed or implied, of a product in any application. Contact your Victaulic sales representative to ensure the best gasket is selected for a particular service. Failure to follow these instructions could cause system failure, resulting in serious personal injury and property damage. Rating Code Key 1 Most Applications 2 Limited Applications 3 Restricted Applications (Nitrile) (EPDM) Grade E (Silicone) GRADE L GRADE T GRADE A GRADE V GRADE O GRADE M (Neoprene) GRADE M2 --- Insufficient Data (White Nitrile) GRADE CHP-2 (Epichlorohydrin) (Fluoroelastomer) (Fluoroelastomer) (Halogenated Butyl) (Hydrogenated Nitrile) Chemical GRADE ST / H Abietic Acid --- --- --- --- --- --- --- --- --- --- Acetaldehyde 2 3 3 3 3 --- --- 2 --- 3 Acetamide 1 1 1 1 2 --- --- 2 --- 3 Acetanilide 1 3 3 3 1 --- --- 2 --- 3 Acetic Acid, 30% 1 2 2 2 1 --- 2 1 2 3 Acetic Acid, 5% 1 2 2 2 1 --- 2 1 1 3 Acetic Acid, Glacial 1 3 3 3 3 --- 3 2 3 3 Acetic Acid, Hot, High Pressure 3 3 3 3 3 --- 3 3 3 3 Acetic Anhydride 2 3 3 3 2 --- 3 3 --- 3 Acetoacetic Acid 1 3 3 3 1 --- --- 2 --- 3 Acetone 1 3 3 3 3 --- 3 3 3 3 Acetone Cyanohydrin 1 3 3 3 1 --- --- 2 --- 3 Acetonitrile 1 3 3 3 1 --- --- --- --- 3 Acetophenetidine 3 2 2 2 3 --- --- --- --- 1 Acetophenone 1 3 3 3 3 --- 3 3 --- 3 Acetotoluidide 3 2 2 2 3 --- --- --- --- 1 Acetyl Acetone 1 3 3 3 3 --- 3 3 --- 3 The data and recommendations presented are based upon the best information available resulting from a combination of Victaulic's field experience, laboratory testing and recommendations supplied by prime producers of basic copolymer materials.
    [Show full text]
  • The Institute of Paper Chemistry
    The Institute of Paper Chemistry Appleton, Wisconsin Doctor's Dissertation Reaction Products of Lignin Model Compounds and Sodium Hydrosulfide Thomas G. Zentner June, 1953 A STUDY OF THE REACTION PRODUCTS OF LIGNIN MODEL COMPOUNDS AND SODIUM HYDROSULFIDE A thesis submitted by Thomas G. Zentner B.S. 1948, Texas A & M College M.S. 1950, Lawrence College in partial fulfillment of the requirements of The Institute of Paper Chemistry for the degree of Doctor of Philosophy from Lawrence College, Appleton, Wisconsin June, 1952 TABLE OF CONTENTS INTRODUCTION 1 HISTORICAL REVIEW 2 PRESENTATION OF THE PROBLEM 8 EXPERIMENTAL PROCEDURES 10 Synthesis of Compounds 10 Synthesis of 1-(4-Hydroxy-3-methoxyphenyl)-l-propanol 10 Synthesis of 1-(4-Benzoxy-3-methoxyphenyl)-l-propanol 11 Reaction of 1-(4-Benzoxy-3-methoxyphenyl) l-propanol with Benzyl Chloride 12 Synthesis of Propiovanillone 14 Synthesis of (-(4-Acetyl-2-methoxyphenoxy)acetovanillone 17 Attempted Synthesis of a-(2-Methoxy-4-methylphehoxy)- propiovanillone 17 Attempted Synthesis of 4-[l-(2-Methoxy-4-methylphenoxy)- l-propyl]guaiacol 21 Synthesis of 2t,4-Dihydroxy-3-methoxychalcone 23 Synthesis of 4,4'-Dihydroxy-3,3 -dimethoxychalcone 24 Synthesis of 4-Propionylpyrocatechol 24 Synthesis of Bis[l-(4-hydroxy-3-methoxyphenyl)-1- propyl] Disulfide 26 Reaction of Isolated Native Lignin with Potassium Hydrosulfide 27 Sodium Hydrosulfide Cooks 28 Cooking Liquor 28 General Procedures 30 Propiovanillone' 32 iii 2 ,4-Dihydroxy-3-methoxychalcone 34 4,4'-Dihydroxy-3,3 '-methoxychalcohe 37 4'-Hydroxy-3t-methoxyflavanone 39 2-Vanillylidene-3-coumaranone 41 Vanillin 44 G- (4-Acetyl-2-methoxyphenoxy)acetovanillone 45 1-(4-Hydroxy-3-methoxyphenyl)-1-propanol 49 DISCUSSION 58 SUMMARY AND CONCLUSIONS 69 LITERATURE CITED 71 INTRODUCTION Although the kraft process has been in use for many years, there is no sound explanation of the role played by the sulfide ion in the cook.
    [Show full text]
  • Chemical Resistance 100% SOLIDS EPOXY SYSTEMS
    Chemical Resistance 100% SOLIDS EPOXY SYSTEMS CHEMICAL 8300 SYSTEM 8200 SYSTEM 8000 SYSTEM OVERKOTE PLUS HD OVERKOTE HD OVERKRETE HD BASED ON ONE YEAR IMMERSION TESTING –––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––––– Acetic Acid (0-15%) G II Acetonitrile LLG L Continuous Immersion Acetone (0-20%) LLL Acetone (20-30%) Suitable for continuous immersion in that chemical (based on LLG Acetone (30-50%) L G I ONE YEAR testing) to assure unlimited service life. Acetone (50-100%) G II Acrylamide (0-50%) LLL G Short-Term Exposure Adipic Acid Solution LLL Alcohol, Isopropyl LLL Suitable for short-term exposure to that chemical such as Alcohol, Ethyl LLG secondary containment (72 hours) or splash and spill Alcohol, Methyl LLI (immediate clean-up). Allyl Chloride LLI Allylamine (0-20%) L L I Allylamine (20-30%) L G I I Not Suitable Allylamine (30-50%) GGI Not suitable for any exposure to that chemical. Aluminum Bromide LL– Aluminum Chloride L L – Aluminum Fluoride (0-25%) L L – This chart shows chemical resistance of our various Aluminum Hydroxide LLL 1 topping materials (90 mils – ⁄4"). These ratings are based on Aluminum Iodide LL– temperatures being ambient. At higher temperatures, chemical Aluminum Nitrate LL– resistance may be effected. When chemical exposure is Aluminum Sodium Chloride L L – minimal to non-existent, a 9000 System–FlorClad™ HD or Aluminum Sulfate LLL 4600 System– BriteCast™ HD may be used. Alums L L L 2-Aminoethoxyethanol Resistance data is listed with the assumption that the material GGG has properly cured for at least four days, at recommended Ammonia – Wet L L – temperatures, prior to any chemical exposure.
    [Show full text]
  • Corrosion-2020) (461 Event of the European Federation of Corrosion)
    European Federation of Corrosion National Academy of Sciences of Ukraine Ministry of Education and Science of Ukraine Ukrainian Association of Corrosionists Karpenko Physico-Mechanical Institute Ivan Franko Lviv National University Ivano-Frankivsk National Technical University of Oil and Gas ХV International Conference «Problems of corrosion and corrosion protection of materials» (Corrosion-2020) (461 event of the European Federation of Corrosion) ABSTRACT BOOK October 15–16, 2020 Lviv, Ukraine UДC 539.3, 620.193, 620.194, 620.179, 620.197, 621.181:669.018, 621.785. XV International Conference “Problems of Corrosion and Corrosion Protection of Materials“ (Corrosion-2020). October 15-16, 2020, Lviv, Ukraine: Book of Abstract / Karpenko Physico-Mechanical Institute of NAS of Ukraine; S. Korniy, М.-О. Danyliak, Yu. Maksishko (Eds.). – Lviv, 2020. – 121 p. XV International Conference “Problems of Corrosion and Corrosion Protection of Materials“ (Corrosion-2020) was held at Lviv Palace of Arts on October 15-16, 2020. This Book of Abstract contains the results of studies are devoted to fundamentals of corrosion and corrosion assisted mechanical fracture; hydrogen and gas corrosion; new corrosion resistant materials; thermal spray, electroplated and other coatings; inhibitor, biocidal and electrochemical protection; testing methods and corrosion control; corrosion protection of oil and gas industry and chemical equipment. In the authors edition. Editorial board: S. Korniy, М.-О. Danyliak, Yu. Maksishko ©Karpenko Physico-Mechanical Institute of NAS of Ukraine, Lviv, 2020 CONFERENCE TOPICS: fundamentals of corrosion and corrosion assisted mechanical fracture; hydrogen and gas corrosion; new corrosion resistant materials and coatings; inhibitor and biocidal protection; electrochemical protection; testing methods and corrosion control; corrosion protected equipment of the oil and gas, chemical and energy industries.
    [Show full text]
  • Traumatic Shock. Ii. the Preparation of Cystine, Methionine, and Homocystine Containing Radioactive Sulfur
    TRAUMATIC SHOCK. II. THE PREPARATION OF CYSTINE, METHIONINE, AND HOMOCYSTINE CONTAINING RADIOACTIVE SULFUR Arnold M. Seligman, … , Alexander M. Rutenburg, Henry Banks J Clin Invest. 1943;22(2):275-279. https://doi.org/10.1172/JCI101393. Research Article Find the latest version: https://jci.me/101393/pdf TRAUMATIC SHOCK. II. THE PREPARATION OF CYSTINE, METHIONINE, AND HOMOCYSTINE CONTAINING RADIOACTIVE SULFUR By ARNOLD M. SELIGMAN, ALEXANDER M. RUTENBURG, AND HENRY BANKS 1 (From the Surgical Research Department of the Beth Israel Hospital and the Department of Surgery, Harvard Medical School, Boston) (Received for publication November 12, 1942) In order to prepare, from radioactive sulfur, the benzyl mercaptan (I) (0.6 moles), reported by sulfur-containing amino acids of a high order of Wood and du Vigneaud (4) in 23 per cent yield, specific activity for biological experiments such was found to give a 21.5 per cent yield when 0.06 as those described in the foregoing publication, it mole was used. Reduction of benzylcysteine was necessary (owing to the cost of radioactive (VIII) to cysteine with sodium and butyl alcohol sulfur) to investigate the efficiency of utilization did not give good yields; therefore, sodium and of small amounts of sulfur. The synthetic meth- liquid ammonia were used. Since radioactive ods utilized are not novel, but are described be- benzyl mercaptan is necessary for the synthesis of low because of the data obtained on yields in all three amino acids, a method of preparation of numerous small scale preparations. Since pres- the mercaptan from hydrogen sulfide, other than ent methods of preparing radioactive sulfur from that described by Tarver and Schmidt, in 70 per neutron bombardment of carbon tetrachloride in- cent yield, was investigated.
    [Show full text]
  • WO 2017/116773 Al 6 July 2017 (06.07.2017) W P O P C T
    (12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization International Bureau (10) International Publication Number (43) International Publication Date WO 2017/116773 Al 6 July 2017 (06.07.2017) W P O P C T (51) International Patent Classification: 85008-3279 (US). SHULT, Nicholas S.; 2255 North 44th C23F 1/14 (2006.01) H05K 3/38 (2006.01) Street, Suite 300, Phoenix, Arizona 85008-3279 (US). C01B 15/08 (2006.01) C09G 1/00 (2006.01) GOLDSMITH, Adam T.; 2255 North 44th Street, Suite 300, Phoenix, Arizona 85008-3279 (US). (21) International Application Number: PCT/US20 16/0673 13 (74) Agent: ROSENFIELD, Susan Stone; Fennemore Craig, 2394 East Camelback Road, Suite 600, Phoenix, Arizona (22) International Filing Date: 85016 (US). 16 December 2016 (16. 12.2016) (81) Designated States (unless otherwise indicated, for every (25) Filing Language: English kind of national protection available): AE, AG, AL, AM, (26) Publication Language: English AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DJ, DK, DM, (30) Priority Data: DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, 62/273,389 30 December 201 5 (30. 12.2015) US HN, HR, HU, ID, IL, IN, IR, IS, JP, KE, KG, KH, KN, 15/380,702 15 December 201 6 (15. 12.2016) US KP, KR, KW, KZ, LA, LC, LK, LR, LS, LU, LY, MA, (71) Applicant: TESSENDERLO KERLEY, INC. [US/US]; MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, 2255 North 44th Street, Suite 300, Phoenix, Arizona NI, NO, NZ, OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, 85008-3279 (US).
    [Show full text]
  • General Chemical Resistance of a Fluoroelastomer Coatings & Sealants Fluoroelastomer
    General Chemical Resistance of a Fluoroelastomer Coatings & Sealants Fluoroelastomer www.pelseal.com Pelseal Technologies’ state-of-the-art fluid coatings, surface area to volume. Therefore, the ratings in the caulks, adhesives and sealants are manufactured from accompanying listing should be used only as a general fluoroelastomer rubber. Our products resist attack, to guide, not as specific recommendations. varying degrees, by a broad spectrum of industrial chemicals, fuels, oils, and other substances. While the information is presented by us in good faith, no guarantee, expressed or implied, can be given regarding We have researched the effect of the listed chemicals the accuracy of these ratings. on fluoroelastomers at various temperatures, concentrations, and exposure times. Our information is based on extensive In those cases where no data are available, the rating laboratory tests and experiments that have been performed shown is the considered, conditional opinion of experienced on fluoroelastomers themselves by a number of outside rubber chemists and compounders. organizations, including manufacturers, end users, suppliers, and trade associations. We strongly urge you to test our products under actual or simulated service conditions, before you purchase them, The information is believed to be reliable. However, the rather than assume that they will perform satisfactorily in degree of fluid resistance of an elastomer to deterioration your specific application. In order to assist you in learning by a specific substance is dependent on many variables, more about the chemical resistance of Pelseal's products including the concentration and temperature of the material; to the substance shown, the following rating code has the frequency and duration of exposure; the velocity of been used: flow and aeration; mechanical action; and the ratio of contact CODE E Excellent Resistance - little or minor attack by the material on fluoroelastomers; 0-5% volume swell where applicable.
    [Show full text]
  • Working with Hazardous Chemicals
    A Publication of Reliable Methods for the Preparation of Organic Compounds Working with Hazardous Chemicals The procedures in Organic Syntheses are intended for use only by persons with proper training in experimental organic chemistry. All hazardous materials should be handled using the standard procedures for work with chemicals described in references such as "Prudent Practices in the Laboratory" (The National Academies Press, Washington, D.C., 2011; the full text can be accessed free of charge at http://www.nap.edu/catalog.php?record_id=12654). All chemical waste should be disposed of in accordance with local regulations. For general guidelines for the management of chemical waste, see Chapter 8 of Prudent Practices. In some articles in Organic Syntheses, chemical-specific hazards are highlighted in red “Caution Notes” within a procedure. It is important to recognize that the absence of a caution note does not imply that no significant hazards are associated with the chemicals involved in that procedure. Prior to performing a reaction, a thorough risk assessment should be carried out that includes a review of the potential hazards associated with each chemical and experimental operation on the scale that is planned for the procedure. Guidelines for carrying out a risk assessment and for analyzing the hazards associated with chemicals can be found in Chapter 4 of Prudent Practices. The procedures described in Organic Syntheses are provided as published and are conducted at one's own risk. Organic Syntheses, Inc., its Editors, and its Board of Directors do not warrant or guarantee the safety of individuals using these procedures and hereby disclaim any liability for any injuries or damages claimed to have resulted from or related in any way to the procedures herein.
    [Show full text]
  • Chemical Resistance Chart
    Polyurethane Thermal-Chem Corp. High Performance Epoxy Topcoats Products Chemical Resistance Chart E56 E = Excellent G = Good F = Fair Clear surfacer Plus 3.0 DecoTop < = Occasional Spillage U = Do Not Use AcidGard VersiGard ArmorTred Resurfacer Resurfacer ArmorClad Resurfacer Re DecoThane ArmorBond SolventGard DecoTop P92 Chemical 750 755 757 728 731 736 705 748 1056 1060 Polyurethane Thermal-Chem Corp. High Performance Epoxy Topcoats Products Chemical Resistance Chart E = Excellent G = Good F = Fair Clear surfacer Plus 3.0 DecoTop < = Occasional Spillage U = Do Not Use AcidGard VersiGard ArmorTred Resurfacer Resurfacer ArmorClad Resurfacer Re ThermalCrete ArmorBond SolventGard DecoFinish P81 Chemical 750 755 757 728 731 736 705 748 1030 1062 1, 4-Dichloro-2-butene U E E U U U U U U U 1, 4-Dioxane U < < U U U U U U U 1-1-1 Trichloroethane E E E F F G G F G G < < < < < 2, 4-Pentanedione F E E F F 3, 4-Dichloro-1-butene < E E U U U U U U U 4-Picoline (0-50%) U < < U U U U U V V Acetic Acid (0-5%) E E E G G G G G E G < < < < < < Acetic Acid (5-15%) E E E F Acetone(0-20%) E E E F G G G G E F Acetone (20-30% < E E < < < < < E < Acetone (30-50%) < E E < < < < < E < Acetone (50-100%) < F F < < < < < E < Acetonitrile F E E < < < < < E < Acrylamide (0-50%) E E E F G G G G F Adipic Acid Solution E E E E E E E E G Alcohol, Ethyl E E E F F F F F F Alcohol, Isopropyl E E E F F F F F G F Alcohol, Methyl < E E < < < < < < < Allyl Chloride < E E U U U U U E < Allylamine (0-20%) < E E U U U U U < Allylamine (20-30%) < E E U U U U U < Allylamine (30-50%) U < < U U U U U U Aluminum Bromate E E E F G G G G E Aluminum Bromide E E E E E E E E E Aluminum Chloride E E E E E E E E E Aluminum Fluoride (25%) E E E E E E E E E Polyurethane Thermal-Chem Corp.
    [Show full text]
  • Choosing the Best Hose and Tube for Your Application Verderflex Tube Selection Choosing the Best Tube for Your Application
    VERDERFLEX Chemical Compatibility Guide Choosing the best hose and tube for your application Verderflex Tube Selection Choosing the best tube for your application The tube is the heart and soul of any peristaltic pump: a poorly selected tube will result in frequent tube changes and increased overall cost of ownership of any equipment. Conventionally, tube size is stated as Internal Diameter (ID) x Wall Thickness (WT). Key Tube Selection Issues Include: Chemical Compatibility Suction Lift Verderprene is an economic, general purpose tubing Suction lift is determined by a combination of the that resists many chemicals whilst offering excellent tube’s ID and WT, ideally the smallest tube diameter dynamic resistance. Some materials have better should be combined with the thickest wall tube and chemical strength at the expense of mechanical life the tube material’s inherent restitution properties. and material cost. Verderprene and Silicone have superior lift capabilities than similar sized materials such as Tygon® or Viton®. Life/Duty Cycle Tubing life is related to the tube’s mechanical Cost strength, the number of compressions and the Most tubing is produced by thermoplastic extrusion, operating cycle. Again, Verderprene is the most hence, tubing cost is related to the raw materials economic solution with the best mechanical life. used. Highly chemical resistive materials like Tygon® and Viton® are more expensive to produce than Verderprene or Silicone. Verderprene® - General Purpose Tubing ▪ Autoclavable and is used in many applications This opaque, cream coloured tube is the most popu- ▪ Good mechanical recovery for optimal suction lar choice for tube pumps having: lift ▪ Medium gas permeability ▪ Best mechanical strength for optimal lifespan ▪ Temp.
    [Show full text]
  • Corrosion Resistance of Titanium
    corrosion resistance of titanium Titanium Metals Corporation TIMET® The world’s complete titanium resource Alloys products expertise Titanium Metals Corporation service inventory TIMET 40 YEAR WARRANTY In most power plant surface condenser tubing, tubesheet and service water pipe applications, TIMET CODEWELD® Tubing and CODEROLL® Sheet, Strip and Plate can be covered by written warranties against failure by corrosion for a period of 40 years. For additional information and copies of these warranties, please contact any of the TIMET locations shown on the back cover of this brochure. The data and other information contained herein are derived from a variety of sources which TIMET believes are reliable. Because it is not possible to anticipate specific uses and operating conditions, TIMET urges you to consult with our technical service personnel on your particular applications. A copy of TIMET’s warranty is available on request. TIMET ®, TIMETAL®, CODEROLL® and CODEWELD® are registered trademarks of Titanium Metals Corporation. FORWARD Since titanium metal first became a This brochure summarizes the commercial reality in 1950, corrosion corrosion resistance data accumulated resistance has been an important in over forty years of laboratory consideration in its selection as an testing and application experience. engineering structural material. The corrosion data were obtained Titanium has gained acceptance using generally acceptable testing in many media where its corrosion methods; however, since service resistance and engineering properties conditions may be dissimilar, TIMET have provided the corrosion and recommends testing under the actual design engineer with a reliable and anticipated operating conditions. economic material. i CONTENTS Forward ........................................................................... i Introduction ...................................................................... 1 Chlorine, Chlorine Chemicals, and Chlorides ...........................
    [Show full text]