CO6170073A1 - ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR GEL AND PIPE CLEANER - Google Patents
ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR GEL AND PIPE CLEANERInfo
- Publication number
- CO6170073A1 CO6170073A1 CO08132110A CO08132110A CO6170073A1 CO 6170073 A1 CO6170073 A1 CO 6170073A1 CO 08132110 A CO08132110 A CO 08132110A CO 08132110 A CO08132110 A CO 08132110A CO 6170073 A1 CO6170073 A1 CO 6170073A1
- Authority
- CO
- Colombia
- Prior art keywords
- concentrator
- tank
- produce
- aqueous polymer
- tanks
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/02—Cleaning pipes or tubes or systems of pipes or tubes
- B08B9/027—Cleaning the internal surfaces; Removal of blockages
- B08B9/04—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes
- B08B9/053—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction
- B08B9/055—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction the cleaning devices conforming to, or being conformable to, substantially the same cross-section of the pipes, e.g. pigs or moles
- B08B9/0555—Gelled or degradable pigs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/59—Mixing systems, i.e. flow charts or diagrams
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/53—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D3/00—Arrangements for supervising or controlling working operations
- F17D3/03—Arrangements for supervising or controlling working operations for controlling, signalling, or supervising the conveyance of several different products following one another in the same conduit, e.g. for switching from one receiving tank to another
- F17D3/05—Arrangements for supervising or controlling working operations for controlling, signalling, or supervising the conveyance of several different products following one another in the same conduit, e.g. for switching from one receiving tank to another the different products not being separated
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Mechanical Engineering (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- Detergent Compositions (AREA)
- Cleaning In General (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Colloid Chemistry (AREA)
Abstract
Proceso en línea para la formación de un gel empleado en la separación de interfaces de fluidos y limpieza de tuberías, caracterizado por: a. mezclar, en un primer tanque concentrador (1), un polímero natural de coma guar, o un derivado del mismo, un modificador de pH y un agente biocida para producir una solución acuosa de polímero; b. mezclar, en un segundo tanque concentrador (2), una sal inorgánica polivalente seleccionada de sales de borato y cromo, sus anhidros e hidratos para producir una solución acuosa de entrecruzante; y c. combinar el producto contenido en dichos primer y segundo tanques concentradores en los mezcladores estáticos (9) de la línea de formación del gel, antes de inyectarlo al oleoducto poliducto. El proceso de la reivindicación 1, caracterizado porque la relación de volúmenes del primer tanque concentrador (1) al segundo tanque concentrador (2) es de 30:1. El proceso de la reivindicación 1, caracterizado porque el proceso de producción de las soluciones acuosas de polímero y de entrecruzante en el primer y el segundo tanque concentrador se lleva a cabo con recirculación. El proceso de la reivindicación 1, caracterizado porque para producir la solución acuosa de polímero se llena el primer tanque concentrador con agua a la cual se le agregan el agente modificador de pH y el biocida y entonces, es recirculada hacia el mismo tanque (1) mediante una bomba (3) por una tubería, en la corriente de recirculación se adiciona el polímero natural con la ayuda de un sistema de dosificación especial (4) y luego, se pasa la mezcla por los mezcladores estáticos (8) antes de entrar nuevamente al tanque (1).Online process for the formation of a gel used in the separation of fluid interfaces and pipe cleaning, characterized by: a. mixing, in a first concentrator tank (1), a natural guar coma polymer, or a derivative thereof, a pH modifier and a biocidal agent to produce an aqueous polymer solution; b. mixing, in a second concentrator tank (2), a polyvalent inorganic salt selected from borate and chromium salts, its anhydrous and hydrates to produce an aqueous solution of crosslinker; and c. combining the product contained in said first and second concentrator tanks in the static mixers (9) of the gel formation line, before injecting it into the polyduct pipeline. The process of claim 1, characterized in that the volume ratio of the first concentrator tank (1) to the second concentrator tank (2) is 30: 1. The process of claim 1, characterized in that the production process of aqueous polymer and crosslinker solutions in the first and second concentrator tanks is carried out with recirculation. The process of claim 1, characterized in that to produce the aqueous polymer solution, the first concentrator tank is filled with water to which the pH modifying agent and the biocide are added and then, it is recirculated to the same tank (1) by means of a pump (3) through a pipe, in the recirculation stream the natural polymer is added with the help of a special dosing system (4) and then, the mixture is passed through the static mixers (8) before entering again to the tank (1).
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CO08132110A CO6170073A1 (en) | 2008-12-12 | 2008-12-12 | ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR GEL AND PIPE CLEANER |
PCT/IB2009/007654 WO2010067168A1 (en) | 2008-12-12 | 2009-11-24 | In-line method for producing a pipeline-cleaning and interface-separating gel |
PE2011001203A PE20120522A1 (en) | 2008-12-12 | 2009-11-24 | ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR AND PIPE CLEANER GEL |
EC2011011122A ECSP11011122A (en) | 2008-12-12 | 2011-06-10 | ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR GEL AND PIPE CLEANER |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CO08132110A CO6170073A1 (en) | 2008-12-12 | 2008-12-12 | ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR GEL AND PIPE CLEANER |
Publications (1)
Publication Number | Publication Date |
---|---|
CO6170073A1 true CO6170073A1 (en) | 2010-06-18 |
Family
ID=42242388
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CO08132110A CO6170073A1 (en) | 2008-12-12 | 2008-12-12 | ONLINE PROCESS FOR THE PRODUCTION OF AN INTERFACE SEPARATOR GEL AND PIPE CLEANER |
Country Status (4)
Country | Link |
---|---|
CO (1) | CO6170073A1 (en) |
EC (1) | ECSP11011122A (en) |
PE (1) | PE20120522A1 (en) |
WO (1) | WO2010067168A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106422955B (en) * | 2016-08-30 | 2019-03-15 | 扬州大学 | It is a kind of quickly, the device and method of a large amount of, continuous production nanoemulsions or nano suspending liquid |
CO2019005808A1 (en) * | 2019-05-31 | 2019-09-30 | Ecopetrol Sa | Process to obtain a hydrocarbon transportable by pipeline composed of heavy and extra-heavy crude oils with non-conventional diluents |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1145902A (en) * | 1979-11-20 | 1983-05-10 | Hydrochem Industrial Services, Inc. | Gelled pigs for cleaning and sanitizing pipelines |
US5346011A (en) * | 1993-04-01 | 1994-09-13 | Halliburton Company | Methods of displacing liquids through pipes |
CA2177506A1 (en) * | 1995-07-26 | 1996-09-27 | Canadian Fracmaster Ltd. | Method and apparatus for forming solid phase plugs in pipelines |
-
2008
- 2008-12-12 CO CO08132110A patent/CO6170073A1/en active IP Right Grant
-
2009
- 2009-11-24 WO PCT/IB2009/007654 patent/WO2010067168A1/en active Application Filing
- 2009-11-24 PE PE2011001203A patent/PE20120522A1/en not_active Application Discontinuation
-
2011
- 2011-06-10 EC EC2011011122A patent/ECSP11011122A/en unknown
Also Published As
Publication number | Publication date |
---|---|
PE20120522A1 (en) | 2012-05-17 |
WO2010067168A1 (en) | 2010-06-17 |
ECSP11011122A (en) | 2011-07-29 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG | Application granted |