US2330051A - Method for the prevention of corrosion - Google Patents

Method for the prevention of corrosion Download PDF

Info

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
Application number
US355521A
Inventor
Heidt Peter
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MEYER A MATHIASEN
Original Assignee
MEYER A MATHIASEN
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by MEYER A MATHIASEN filed Critical MEYER A MATHIASEN
Priority to US355521A priority Critical patent/US2330051A/en
Application granted granted Critical
Publication of US2330051A publication Critical patent/US2330051A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23FNON-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
    • C23F15/00Other methods of preventing corrosion or incrustation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1266Inorganic 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

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.
US355521A 1940-09-05 1940-09-05 Method for the prevention of corrosion Expired - Lifetime US2330051A (en)

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
US (1) US2330051A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
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

Cited By (8)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US4039717A (en) Method for reducing the adherence of crude oil to sucker rods
US2330051A (en) Method for the prevention of corrosion
US3794472A (en) Method for preventing the freezing together of coal particles
US2151353A (en) Composition for treating ferrous metals
US2241493A (en) Protecting coating
US2907717A (en) Breaking crude oil emulsions
US4160063A (en) Method for preventing the adherence of oil to surfaces
US3062684A (en) Method of inhibiting corrosion of iron and steel
US2385175A (en) Pipe-line corrosion inhibition
US3002909A (en) Method of inhibiting corrosion
US3281268A (en) Scale removal
US3563714A (en) Methods and compositions for packing coal
US2126430A (en) Method of treating ships' tanks and other large containers to protect their interior surfaces against corrosion
US3050360A (en) Method of inhibiting corrosion of iron and steel
US3895910A (en) Method of protecting tin-packaging against corrosion and making them glossy
US3067069A (en) Removal of liquid hydrocarbons from empty compartments of ocean-going tankers
US1109670A (en) Method of preparing steel for painting.
US3822998A (en) Method of protecting tin-packings against corrosion and making them glossy
DE2504990A1 (en) PROCESS FOR PREPARING METAL SURFACES FOR THE APPLICATION OF PROTECTIVE COATINGS
NO129094B (en)
US1344338A (en) Rust-preventing solution and process of preparing the same
US1796310A (en) Method of treating lubricants
US2973314A (en) Process for dehazing petroleum hydrocarbons with solid sodium silicate
USRE18988E (en) Method of treating lubricants
US2042412A (en) Process for the preparation of inhibitors