US2330051A - Method for the prevention of corrosion - Google Patents
Method for the prevention of corrosion Download PDFInfo
- Publication number
- US2330051A US2330051A US355521A US35552140A US2330051A US 2330051 A US2330051 A US 2330051A US 355521 A US355521 A US 355521A US 35552140 A US35552140 A US 35552140A US 2330051 A US2330051 A US 2330051A
- Authority
- US
- United States
- Prior art keywords
- tank
- corrosion
- compartment
- tanks
- metal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F15/00—Other methods of preventing corrosion or incrustation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1266—Inorganic compounds nitrogen containing compounds, (e.g. NH3)
Definitions
- My improved process consists in releasing from one-third of an ounce to one ounce of ammonia gas (N'Hs), or from one ounce to three ounces of ammonium hydroxide (NHiOH) in the 40 container, the metal of which is to be treated, for each one thousand cubic feet of enclosed tank space.
- N'Hs ammonia gas
- NHiOH ammonium hydroxide
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Description
Patented Sept. 21, 1943 UNITED STATES PATENT OFFICE METHOD FOR THE PREVENTION OF CORROSION 7 Peter Heidt, Philadelphia, Pa., assignor to Meyer A. Mathiasen, Philadelphi aPa.
No Drawing. Application September 5, 1940,
Serial N0. 355,521
8 Claims.
. carry and store acid forming substances and materials such as petroleum, vegetable oils, animal fats, etc.
The problem of preventing and removing cor- 'rosion from steel and other ferrous metal tanks 10 V I than ammonia gas, althoughthe process is not and containers is expensive and tedious according to present known processes. That is particularly true where the containers are adapted to receive acid forming materials, the residue of which it is desired to remove from the tank after emptying of the tank, by means of washing with salt seawater. Thus, it is conventional to remove residue materials from cargo tanks and oil tankers by washing them clean with salt sea water, by hand or mechanical means. In such cases the corrosion is violent and reaches its maximum destructive force shortly after the salt sea water has contacted the metal container. The present cheapest known method of removing residue materials from cargo tanks and oil tankers, etc. is to wash the interior of the container and then treat it with lime. For immunizing or neutralizing a sea-going oil tanker of approximately one million cubic feet internal space this conventional method of treatment would necessitate an expenditure of $75 for lime, I and in addition require approximately one hundred and twenty man hours of labor. With my improved process a tank oi. the same capacity can be emciently treated at a cost not exceeding $2.
My improved process consists in releasing from one-third of an ounce to one ounce of ammonia gas (N'Hs), or from one ounce to three ounces of ammonium hydroxide (NHiOH) in the 40 container, the metal of which is to be treated, for each one thousand cubic feet of enclosed tank space. This application must be made immediately after complete discharge of the liquid cargo in bulk, or upon discharge of ballast, or
immediately after washing the residue from the tank or compartment. This application will neutralize acids over the entire internal surface of the tank or compartment in a few minutes. Unlike conventional processes, mechanical or manual application is not necessary, since the inherent nature of the materials used produce their own locomotion and application. That is, the ammonia gas in the damp compartment, since it has an affinity for water, will penetrate and impregnate the scale and pores of the metal of the tank within a few minutes and completely neutralize all acids from forming. The scale and porous metal of the container will retain the ammonia gases indeflnite1y.- I 1 The composition does not.require,-"in order to be effective, the addition of any other chemicals than those specified, nor is heat treatment necessary in order to render the process efiective.
I'prefer to use ammonium hydroxide rather restricted to the former. That is true because commercially ammonium hydroxide is the more feasible. I
The limitations and proportions of the materials specified are important and critical, within the ranges given, because the use of smaller quantities would be insufficient to render the process effective in neutralizing acids, and the use of larger quantities would enhance an alkali corrosion, which would be even more destruc-' tive than an acid corrosion.
I am well aware that heretofore it has been proposed to apply corrosion resistant coatings to iron and steel by treating them with complicated purpose of preventing corrosion, particularly in the mode herein specified.
Various changes in the ingredients, the proportions specified, and in the steps of the process herein outlined may be made to the invention herein designated without departing from the spirit of the invention or scope of the claims.
I claim:
l. The process of treating the interior of tanks and other containers normally adapted to receive acid forming substances, for the purpose of neutralizin'g the acids and rendering the metal of the tank resistant to the action of rust promoting agents, which consist in freely releasing into the interior of the tank ammonium hydroxide in quantity sufiicient to permit the ammonia gas "therein to permeate and impregnate any scale present and the pores of the metal for preventing and neutralizing acid formations.
eration treating the compartment within the tank with an ammonia gas freely released the interior of metal tanks normally adapted to receive acid forming materials such as petroleum I products; vegetable oils, animal fats, etc., which consist in freely releasing ammonia gas into the compartment of the tank immediately after removal of the acid forming material in amount necessary to prevent the corrosion.
4. The process of preventing the corrosion of the interior of metal tanks normally adapted to receiveacid'forming materials such as petroleum products, vegetable oils, animal fats, etc., which consist in freely releasing ammonia gas into the compartmentof the tank immediately after removal of the acidforming material, in the proportions of from one third of an ounce to one ounce of the ammonia ga to each one thousand cubic feet of treated enclosed tank space.
5. The process of rendering the internal compartment walls of metal tanks (suchas cargo emptying the cargo load from the compartment 'of the tank, thereafter washing the interior of the tank, and immediately after the washing optanks) resistant to corrosion, which consists in therein.
6. The process of rendering the internalcompartment walls of metal tanks (such as cargo tanks) resistant to corrosion, which consists in emptying the cargo load from the compartment of the tank,thereafterwashing the interior of .the tank, and immediately after the washing operation releasin ammonium hydroxide into the compartment within the tank.
7. The process of rendering the internal compartment walls of metal tanks (such as cargo tanks) resistant to corrosion. whichconsists in emptying the'cargo load from the compartment of the tank, thereafter washing the interior of the tank, and immediately after the washing operation freely releasing into the compartment within the tank an ammonia gas in the proportions of from one-third of an ounce to one ounce to each one thousand cubic feet of enclosed compartment space."
8. The process of rendering the internal compartment walls of metal tanks (such as cargo tanks) resistant to corrosion, which consists in emptying the cargo load from the compartment of the tank, thereafter washing the interior of the tank, and immediately after the washing operation releasing into the compartment within the tank ammonium hydroxide in the proportion of from one ounce to three ounces of ammonium hydroxide to each one thousand cubic feet of the enclosed compartment space. I
a, Y PE'IER' HEIDT.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US355521A US2330051A (en) | 1940-09-05 | 1940-09-05 | Method for the prevention of corrosion |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US355521A US2330051A (en) | 1940-09-05 | 1940-09-05 | Method for the prevention of corrosion |
Publications (1)
Publication Number | Publication Date |
---|---|
US2330051A true US2330051A (en) | 1943-09-21 |
Family
ID=23397740
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US355521A Expired - Lifetime US2330051A (en) | 1940-09-05 | 1940-09-05 | Method for the prevention of corrosion |
Country Status (1)
Country | Link |
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US (1) | US2330051A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2422515A (en) * | 1943-09-15 | 1947-06-17 | Standard Oil Co | Prevention of corrosion in ferrous metal pipe lines carrying refined petroleum distillates |
US2522430A (en) * | 1945-07-02 | 1950-09-12 | Standard Oil Dev Co | Suppression of corrosion |
US2566887A (en) * | 1949-10-07 | 1951-09-04 | Continental Can Co | Corrosion inhibitor |
US2634223A (en) * | 1949-07-01 | 1953-04-07 | Standard Oil Dev Co | Method for inhibiting corrosion in storage vessels |
US2639971A (en) * | 1949-01-29 | 1953-05-26 | Standard Oil Dev Co | Inhibiting storage tank corrosion |
US2755166A (en) * | 1951-12-22 | 1956-07-17 | Pure Oil Co | Method of reducing vapor zone corrosion |
US2816812A (en) * | 1952-12-29 | 1957-12-17 | Phillips Petroleum Co | Ammonia corrosion inhibitor feed system |
US3088983A (en) * | 1957-06-17 | 1963-05-07 | Celanese Corp | Conditioning of activated carbon |
-
1940
- 1940-09-05 US US355521A patent/US2330051A/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2422515A (en) * | 1943-09-15 | 1947-06-17 | Standard Oil Co | Prevention of corrosion in ferrous metal pipe lines carrying refined petroleum distillates |
US2522430A (en) * | 1945-07-02 | 1950-09-12 | Standard Oil Dev Co | Suppression of corrosion |
US2639971A (en) * | 1949-01-29 | 1953-05-26 | Standard Oil Dev Co | Inhibiting storage tank corrosion |
US2634223A (en) * | 1949-07-01 | 1953-04-07 | Standard Oil Dev Co | Method for inhibiting corrosion in storage vessels |
US2566887A (en) * | 1949-10-07 | 1951-09-04 | Continental Can Co | Corrosion inhibitor |
US2755166A (en) * | 1951-12-22 | 1956-07-17 | Pure Oil Co | Method of reducing vapor zone corrosion |
US2816812A (en) * | 1952-12-29 | 1957-12-17 | Phillips Petroleum Co | Ammonia corrosion inhibitor feed system |
US3088983A (en) * | 1957-06-17 | 1963-05-07 | Celanese Corp | Conditioning of activated carbon |
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