GB2073357A - A system for cleaning tube- type heat exchangers automatically during operation - Google Patents

A system for cleaning tube- type heat exchangers automatically during operation Download PDF

Info

Publication number
GB2073357A
GB2073357A GB8110658A GB8110658A GB2073357A GB 2073357 A GB2073357 A GB 2073357A GB 8110658 A GB8110658 A GB 8110658A GB 8110658 A GB8110658 A GB 8110658A GB 2073357 A GB2073357 A GB 2073357A
Authority
GB
United Kingdom
Prior art keywords
tube
helix
wire
corrosion
fluid
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.)
Granted
Application number
GB8110658A
Other versions
GB2073357B (en
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.)
Elf Antar France
Original Assignee
Elf France SA
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 Elf France SA filed Critical Elf France SA
Publication of GB2073357A publication Critical patent/GB2073357A/en
Application granted granted Critical
Publication of GB2073357B publication Critical patent/GB2073357B/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/086Heat exchange elements made from metals or metal alloys from titanium or titanium alloys
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/02Cleaning pipes or tubes or systems of pipes or tubes
    • B08B9/027Cleaning the internal surfaces; Removal of blockages
    • B08B9/04Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes
    • B08B9/043Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved by externally powered mechanical linkage, e.g. pushed or drawn through the pipes
    • B08B9/0436Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved by externally powered mechanical linkage, e.g. pushed or drawn through the pipes provided with mechanical cleaning tools, e.g. scrapers, with or without additional fluid jets
    • EFIXED CONSTRUCTIONS
    • E03WATER SUPPLY; SEWERAGE
    • E03CDOMESTIC PLUMBING INSTALLATIONS FOR FRESH WATER OR WASTE WATER; SINKS
    • E03C1/00Domestic plumbing installations for fresh water or waste water; Sinks
    • E03C1/12Plumbing installations for waste water; Basins or fountains connected thereto; Sinks
    • E03C1/30Devices to facilitate removing of obstructions in waste-pipes or sinks
    • E03C1/304Devices to facilitate removing of obstructions in waste-pipes or sinks using fluid under pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • F28F13/125Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation by stirring
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G1/00Non-rotary, e.g. reciprocated, appliances
    • F28G1/06Non-rotary, e.g. reciprocated, appliances having coiled wire tools, i.e. basket type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0059Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for petrochemical plants

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Public Health (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Cleaning In General (AREA)

Abstract

A tube assembly through which a fluid is to flow and containing a device for cleaning the tube and/or preventing the accumulation of deposits therein, the device consisting of a helix 2 of a material which is resistant to corrosion and abrasion, which can be constantly agitated and thus repeatedly brought into contact with the internal walls of the tube 1 under the effect of the fluid stream, the helix 2 being held in position against longitudinal movement by a hook 4 disposed at the upstream end of the helix 2 which hook permits rotation of the helix 2 within the tube 1. <IMAGE>

Description

SPECIFICATION A system for cleaning tube-type heat exchangers automatically during operation The accumulation of dirt and the like in a heat exchanger, for example in oil refineries, entails various drawbacks, such as: -a progressive fall in thermal exchange performance, giving rise to a greater consumption of energy, -a progressive increase in the loss of pressure, and sometimes a limitation on throughput, -the necessity of stopping a plant in order to clean one of its exchangers if it is not fitted with a bypass, which involves a production loss which has to be made up and various expenses inherent in all stopping and restarting operations, such as the expense of fuel, flaring, etc.
Investment in the provision of a bypass involves other expenses, e.g. those of installing isolating valves for the bypass and its valve, as well as those related to the loss of heat during the period when the bypassed exchanger is being cleaned.
In any case, the cleaning of the assembly of heat exchanger tubes is laborious and the dirty tubes are sometimes found to be corroded under the deposit of dirt.
The subject of the invention is a simple, relatively inexpensive device for providing permanent automatic cleaning of the inside of tubes when the exchanger is in use. This device is placed in each tube in the apparatus.
According to one aspect of the invention there is provided a tube assembly through which a fluid is to flow and containing a device for cleaning the tube and/or preventing the accumulation of deposits therein, the device consisting of a helix of a material which is resistant to corrosion and abrasion, which can be constantly agitated and thus repeatedly brought into contact with the internal walls of the tubes under the effect of the fluid stream the helix being held in position against longitudinal movement by a hooking means disposed at the upstream end of the helix, which permits rotation of the helix within the tube.
According to another aspect of the invention there is provided a device for installation within a tube through which a fluid is to flow to clean the tube or to prevent the accumulation of deposits within the tube, the device comprising a helix of corrosion and abrasion resistant wire having means enabling it to be attached to the tube to prevent longitudinal movement but to allow rotation, relative to the tube.
According to a first embodiment, a metal wire in an elongated spiral shape, having a specific pitch varying from 1 to 7 times the diameter of the tube and possibly obtained by stretching a helical spring, is threaded by suction, for example, into a slightly longer tube, to allow for the lengthening of the helical wire during use.
The helix is formed from a metal wire with a diameter of from 0.3 to 1 mm which is resistant to corrosion and abrasion, such as a spring wire made of a suitable metal or alloy such as cold-rolled titanium, for example, or any other suitable material. The choice of the characteristics of the helix-its pitch, diameter, elasticity, the diameter of the wire from which the helix is formed, and the construction material-is basically determined by the vibration frequency desired under the operating conditions of the exchanger.
The elongated helix is bounded by an imaginary cylinder with a diameter which is equal to at least half the diameter of the tube, and it is preferably bounded by an imaginary cylinder with a diameter of between 0.50 and 0.90 times the internal diameter of the tube.
The helix is fixed in the tube in a flexible manner by one of its ends, on the upstream side relative to the flow of fluid, via a hooking system which may be of the same kind as the spring, or of a different kind. Thus this hooking system may be an inserted part, such as a metal hook in the shape of a "U" made of the same material as the spring or any other material which is resistant to corrosion and abrasion. Again, it may be formed by the interlocking connection of the ends of two adjacent wires.
Under the effect of a turbulent stream of fluid, the helix is permanently agitated; it regularly strikes and rubs all the points of the internal wall of the tube as it turns, thus providing repeated contact with the internal wall. A variation in the throughput of the conducted fluid brings about a variation in the length of the arrangement and consequently changes the striking and rubbing points on the interior of the tube.
The invention is illustrated by the following drawings and Examples which are given as an indication, but are not limitative.
Figure 1 shows part of a plate in which the heat exchanger tubes are inserted, shown by their cross-section.
Figure 2 shows a section through the layout of the laboratory test arrangement.
Figure 3 is a schematic section through a heat exchanger in a plant.
Example 1 As shown in Fig. 2, the test was carried out in the laboratory on a glass tube 1 with an internal diameter of 1 5 mm. The helix 2 is formed from a titanium wire with a diameter of 0.5 mm to avoid any risk of corrosion in use. The pitch 3 of the helix is 30 mm.
The diameter of the helix is 11 mm, and it is attached by a hook 4 to the upstream end of the tube.
The fluid chosen is water, so as to enable the behaviour of the stretched spring to be observed in a transparent medium, and it is circulating in the direction indicated by the arrows.
It was thus possible to confirm that at a flow speed of 20 I/minute, analogous to that of the crude oil in the tubes of a specific heat exchanger which regularly becomes soiled, the metal wire is endowed with a permanent agitation motion which brings it into contact with the walls of the tube.
Example 2 An industrial test on a hundred tubes 10 arranged as shown in Fig. 1, with an internal diameter of 1 5 mm, was carried out with a spiralled titanium wire with a diameter of 0.5 mm. The diameter of the helix was 8 mm, and its pitch was 30 mm. These wires were attached at one end either by a hook or by twisting them together in pairs. The crude petroleum circulates at a flow speed of approximately 0.40 m/sec in the tubes.
After operating for approximately 240 days, some of the tubes equipped with helical wires and some other tubes which were not so equipped were removed.
After having cut a certain number of these tubes in half lengthwise, it was possible to observe that the tubes which were equipped with a helix displayed a clean internal wall, while the other tubes were soiled internally.
Example 3 An industrial test on a complete heat exchanger with 2 sets of tubes with an internal diameter of 1 5 mm was carried out with helical titanium wire with a wire diameter of 0.6 mm, a helix diameter of 8 mm and pitch of 30 mm. These wires were attached at the end where the petroleum enters, by a hook, also made of titanium. The crude petroleum circulates in the tubes at a flow speed of approximately 0.40 m/sec.
After an operatihg time of approximately 140 days, the soiling in the tubes of this exchanger was compared with that in an identical exchanger with the same use. The tubes of the exchanger which was not equipped displayed marked internal soiling. A series of comparative measurements of the levels of heat transfer of these two exchangers shows the advantage of the helical device.
It was confirmed that the thermal exchanger equipped with the automatic cleaning device according to the invention maintained its thermal performance, while the exchanger without the arrangement displayed a progressive reduction in its performance, due to progressive soiling.
The device according to the invention therefore makes it possible to avoid the loss of calorific energy and to maintain a maximum and constant level of thermal transfer over a period of time. Another economic advantage is afforded by the fact that the price of supplying and fitting the device is of the same order of magnitude as the cost of cleaning the exchanger, and the investment may be recouped very rapidly by savings in energy and the elimination of cleaning costs.

Claims (7)

1. A tube assembly through which a fluid is to flow and containing a device for cleaning the tube and/or preventing the accumulation of deposits therein, the device consisting of a helix of a material which is resistant to corrosion and abrasion, which can be constantly agitated and thus repeatedly brought into contact with the internal walls of the tube under the effect of the fluid stream, the helix being held in position against longitudinal movement by a hooking means disposed at the upstream end of the helix, which means permits rotation of the helix within the tube.
2. A tube assembly according to Claim 1, wherein the helix is bounded by a notional cylinder with a diameter lying from 50 to 90 percent of the internal diameter of the tube.
3. A tube assembly according to Claim 1, wherein the helix is formed of a metal wire which is resistant to corrosion and abrasion.
4. A tube assembly according to Claim 3, wherein the wire is spring wire of cold-rolled titanium.
5. A tube assembly according to any preceding claim wherein the hooking means is a U-shaped hook.
6. A heat exchanger, including tube assemblies according to any preceding claim.
7. A device for installation within a tube through which a fluid is to flow to clean the tube or to prevent the accumulation of deposits within the tube, the device comprising a helix of corrosion and abrasion resistant wire having means enabling it to be attached to the tube to prevent longitudinal movement but to allow rotation, relative to the tube
GB8110658A 1980-04-08 1981-04-06 System for cleaning tube-type heat exchangers automatically during operation Expired GB2073357B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8007856A FR2479964A1 (en) 1980-04-08 1980-04-08 SELF-CLEANING SYSTEM ON TUBE COIL EXCHANGERS

Publications (2)

Publication Number Publication Date
GB2073357A true GB2073357A (en) 1981-10-14
GB2073357B GB2073357B (en) 1984-06-06

Family

ID=9240629

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8110658A Expired GB2073357B (en) 1980-04-08 1981-04-06 System for cleaning tube-type heat exchangers automatically during operation

Country Status (7)

Country Link
BE (1) BE888308A (en)
DE (1) DE8110199U1 (en)
ES (1) ES264968Y (en)
FR (1) FR2479964A1 (en)
GB (1) GB2073357B (en)
IT (1) IT1137667B (en)
LU (1) LU83284A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2569829A1 (en) * 1984-08-31 1986-03-07 Raffinage Cie Francaise METHOD AND MECHANICAL DEVICE FOR IMPROVING THERMAL TRANSFERS AND PREVENTING THE INJECTION OF HEAT EXCHANGERS
FR2592924A1 (en) * 1986-01-10 1987-07-17 Total France DEVICE FOR HOLDING THE END OF A MOBILE ELEMENT IN A POSITION, ROTATING DRIVE IN A TUBE AND APPLICATION TO PREVENTING FOULING AND CLEANING OF THIS TUBE.
CN101210791B (en) * 2006-12-29 2010-11-10 北京华夏英蓝科技发展有限公司 Self-cleaning reinforcement heat transfer low flow resistance rotor in heat-transfer pipe

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19544185C2 (en) * 1995-11-28 1998-08-13 Renzmann Und Gruenewald Gmbh Heat exchanger
FR2820197B1 (en) 2001-01-30 2006-01-06 Elf Antar France DEVICE REDUCING THE ENCRASSMENT OF A TUBULAR THERMAL EXCHANGER
FR2940152B1 (en) 2008-12-19 2011-01-21 Total Raffinage Marketing DEVICE FOR REDUCING ENCRASSMENT WITHIN A TUBE
CN102128560B (en) * 2011-04-19 2012-10-17 北京化工大学 Twisted belt type pendant in heat exchange pipe

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE389314A (en) *
US3409470A (en) * 1966-06-27 1968-11-05 Dow Chemical Co Cyclic water hammer method
JPS5535912A (en) * 1978-09-06 1980-03-13 Mitsui Toatsu Chemicals Pipe inside scratchinggoff device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2569829A1 (en) * 1984-08-31 1986-03-07 Raffinage Cie Francaise METHOD AND MECHANICAL DEVICE FOR IMPROVING THERMAL TRANSFERS AND PREVENTING THE INJECTION OF HEAT EXCHANGERS
EP0174254A1 (en) * 1984-08-31 1986-03-12 Compagnie De Raffinage Et De Distribution Total France Mechanical device to improve the transfer of heat and to prevent clogging of heat exchangers
FR2592924A1 (en) * 1986-01-10 1987-07-17 Total France DEVICE FOR HOLDING THE END OF A MOBILE ELEMENT IN A POSITION, ROTATING DRIVE IN A TUBE AND APPLICATION TO PREVENTING FOULING AND CLEANING OF THIS TUBE.
EP0233092A1 (en) * 1986-01-10 1987-08-19 COMPAGNIE DE RAFFINAGE ET DE DISTRIBUTION TOTAL FRANCE: Société Anonyme dite Device for maintaining in position one extremity of a mobile element, rotating in a tube, and application for this device
US4781245A (en) * 1986-01-10 1988-11-01 Compagnie De Raffinage Et De Distribution Total France Device for positioning a rotatable element within a tube
CN101210791B (en) * 2006-12-29 2010-11-10 北京华夏英蓝科技发展有限公司 Self-cleaning reinforcement heat transfer low flow resistance rotor in heat-transfer pipe

Also Published As

Publication number Publication date
FR2479964B1 (en) 1982-05-14
IT1137667B (en) 1986-09-10
BE888308A (en) 1981-07-31
GB2073357B (en) 1984-06-06
ES264968U (en) 1983-01-01
DE8110199U1 (en) 1981-10-15
ES264968Y (en) 1983-07-01
LU83284A1 (en) 1981-07-23
IT8120981A0 (en) 1981-04-08
FR2479964A1 (en) 1981-10-09

Similar Documents

Publication Publication Date Title
US4583585A (en) System for cleaning tube-type exchangers automatically during operation
US3319710A (en) Apparatus for cleaning surface condenser and heat exchanger tubes
US8225848B2 (en) Device for reducing fouling in a tubular heat exchanger
US4102393A (en) Heat exchange apparatus
JP4937133B2 (en) Tubular member cleaning scraper
GB2073357A (en) A system for cleaning tube- type heat exchangers automatically during operation
CN1021080C (en) Method of and apparatus for cleaning liquid circling-running tube and use of same in heat exchanger
US7386908B2 (en) Structured foam pig
CN208520252U (en) A kind of heat exchanger tube with self-cleaning and enhanced heat exchange function
WO2006088432A1 (en) Device for cleaning tubes
US3135322A (en) Liquid cooled condenser
KR20230157562A (en) Tube cleaning apparatus used in heat exchanger
CS268801B2 (en) Device for energy transfer in desulphurization system
NO167327B (en) PROCEDURE AND DEVICE FOR AUTOMATIC CLEANING OF A HEAT EXCHANGE FOR GASIC FLUIDS.
US4545426A (en) Reversing turbulators for heat exchangers
IL35375A (en) Heat exchanger and method of operation thereof
CN1948887A (en) Scale spiral line fluidization on line washing in horizontal pipe and heat transferring streng thening device thereof
CN209109757U (en) A kind of phosphoric acid pipeline transportation cleaning device
US7275429B2 (en) Mechanical self-cleaning probe via bi-metallic or shape memory
DE19544185A1 (en) Industrial heat exchanger with tube bundle inserts
JPH0642893A (en) Cleaner for heat exchanger
ES2415908T3 (en) Device for reducing fouling inside a tube
SU1322064A1 (en) Shell-and-tube heat exchanger
SU817478A1 (en) Apparatus for cleaning inner surfaces of straight-pipe heat exchanger pipe
CN219798030U (en) Tubular heat exchanger

Legal Events

Date Code Title Description
PE20 Patent expired after termination of 20 years

Effective date: 20010405