CN101305255A - Heat exchanger, in particular exhaust gas heat exchanger - Google Patents

Heat exchanger, in particular exhaust gas heat exchanger Download PDF

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Publication number
CN101305255A
CN101305255A CNA2006800420459A CN200680042045A CN101305255A CN 101305255 A CN101305255 A CN 101305255A CN A2006800420459 A CNA2006800420459 A CN A2006800420459A CN 200680042045 A CN200680042045 A CN 200680042045A CN 101305255 A CN101305255 A CN 101305255A
Authority
CN
China
Prior art keywords
heat exchanger
coating
manufacture method
coating comprises
described coating
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.)
Pending
Application number
CNA2006800420459A
Other languages
Chinese (zh)
Inventor
克劳斯·菲施勒
迪特尔·格罗斯
欧利韦尔·芒贝
马蒂亚斯·普菲策尔
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.)
Mahle Behr GmbH and Co KG
Original Assignee
Behr GmbH and Co KG
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 Behr GmbH and Co KG filed Critical Behr GmbH and Co KG
Publication of CN101305255A publication Critical patent/CN101305255A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • F28F19/02Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
    • F28F19/06Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings of metal
    • 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
    • F28F19/02Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Paints Or Removers (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

The invention relates to a heat exchanger, in particular an exhaust gas heat exchanger, having at least one surface which is impinged on by a medium, in particular exhaust gas, is made from metal, in particular aluminium or stainless steel, and is provided with a coating. In order to improve the properties of the coating, according to the invention, the coating comprises a coating material based on nanotechnology.

Description

Heat exchanger, particularly exhaust-heat exchanger
Technical field
The present invention relates to a kind of heat exchanger, particularly relate to a kind of heat exchanger that has at least one metal surface, especially aluminium or high-quality steel surface, medium is its surface of backblast especially, and the surface of this heat exchanger has coating.The invention still further relates to a kind of method of making above-mentioned heat exchanger.
Background technology
In exhaust-heat exchanger, mainly come from the waste gas of diesel engine, with moisture and temperature acting in conjunction, make used metal be subjected to corrosion failure.Can adopt heat-resisting paint for preventing corrosion.
Summary of the invention
The manufacture method that the purpose of this invention is to provide a kind of heat exchanger and realize above-mentioned heat exchanger.Particularly a kind of at least one metal surface that has of this heat exchanger, especially the heat exchanger on the surface of aluminium or high-quality steel, medium is its surface of backblast especially, and the surface of this heat exchanger has coating, and described coating has more excellent characteristic than traditional coating.
The object of the present invention is achieved like this: a kind of heat exchanger, particularly a kind of at least one metal surface that has, especially the heat exchanger on the surface of aluminium or high-quality steel, medium is its surface of backblast especially, the surface of this heat exchanger has coating, described coating comprises a kind of coating material based on nanometer technology, and preferred, coating comprises at least a nano material or nanostructured.Coating is transparent, and has extraordinary chemical corrosion resistance.
A preferred embodiment of heat exchanger of the present invention is characterised in that described coating comprises a kind of key component of being made up of organic principle and inorganic constituents.Under the effect of crosslinking temperature, can in relative broad range, define and change the properties of materials of coating.
Another preferred embodiment of heat exchanger of the present invention is characterised in that coating contains silicon.Preferably, by using suitable catalyst, when decomposing ethanol, hydrolysis organic (alkoxyl) silane on purpose.
Another preferred embodiment of heat exchanger of the present invention is characterized in that coating comprises titanium, zirconium, aluminium, magnesium, zinc, and/or calcium.Different materials constitutes specific inorganic network structure.
In the manufacture method of above-mentioned heat exchanger, particularly exhaust-heat exchanger, aforesaid purpose is achieved in that coating is to be produced by the process that colloidal sol and gel state are changed mutually.Change in the process of gel at colloidal sol, produce nano material.By hydrolysis and concentration response, produce a kind of three-dimensional netted thing that the molecule interlayer is arranged in the liquid, heat treatment process makes gel further be converted into nano material or nanostructured.
A preferred embodiment of manufacture method of the present invention is characterised in that at least a colloidal sol is used to the surface that will apply.The surface that applies can impregnated in the colloidal sol in any suitable manner.
Another preferred embodiment of manufacture method of the present invention is characterised in that colloidal sol is treated, and preferred processing method is heat treatment.
Another preferred embodiment of manufacture method of the present invention comprises the steps: to make the heat exchanger that needs to apply to be immersed in the coating material, then it is drained; Heat exchanger after draining heats in a drying oven.The heat exchanger that need apply is forced to be immersed in the coating material, and then drain.Preferably, again heat exchanger is hung,, and can not form undesired accumulation in inside so that all excess coating materials can flow out.The drop matter that sticks to heat exchanger outlet can be removed by suitable mode, for example can remove by compressed air or electrostatic drop removal device.
Describe different embodiment below in detail, further describe advantage of the present invention, feature and detailed description.Here each technical characterictic of mentioning of claim and specification or separately or combination arbitrarily all has essential meaning for purposes of the invention.
The present invention relates to a kind of heat exchanger, make by aluminium or high-quality steel.This heat exchanger has a cavity, and waste gas flows through this cavity when heat exchanger operates.Described cavity scribbles the coating material based on nanometer technology.This coating material main component comprises inorganic constituents and organic principle.Under the effect of crosslinking temperature, can in relative broad range, limit the characteristic of coating.When furnace temperature was high, the more a high proportion of content of organic matter was discharged from, and that is to say to have crosslinkedly greatly, so the erosion resisting of coating is enhanced.When furnace temperature was low, the ratio of the content of organic matter was bigger, that is to say, it is better that the ductility of coating becomes.
According to one aspect of the present invention, the heat exchanger that need apply is forced to be immersed in the coating material, and then drain.Afterwards heat exchanger is hung,, and can not form accumulation in inside so that the excess coating material drains fully.The drop matter that sticks to outlet can be removed by suitable mode, for example can remove by compressed air or electrostatic drop removal device.Exhaust-heat exchanger is by a drying oven then.
Here, coating produces by a sol-gel process, for example, and so-called ORMOCER coating.ORMOCER is meant a trade mark at the Fraunhofer Gesellschaft of Munich development and application research.In order to obtain coating, by using suitable catalyst, make the organosilan hydrolysis, thereby make as methyl alcohol, alcohol such as ethanol decomposes.Concentration response subsequently will cause the organically-modified formation of inorganic oxide structure.For inorganic netted modification, silicon also can the part by other element substitutions, particularly titanium, zirconium or aluminium element.In addition, magnesium, zinc, calcium may be incorporated in together.Water-soluble alcohol colloidal sol is applied on the heat exchanger that will apply in the dip-coating process, again through heat treatment.Form cross-linked polymeric layer like this.
Coating can also prevent dust, particulate, the adhesion of cigarette ash and oil film simultaneously except anticorrosion and waterproof effect.When using " ORMOCER " coating, the composition of fluorosilicone accounts for 0.1 to 10% of ORMOCER coating, and preferably 0.5 to 5%, particularly contain at 1 to 2% o'clock, the effect of this oleophobic just can realize.The alkoxy silane that has a highly fluorinated alkyl chain by interpolation can obtain the binder course of the characteristic of hydrophobic simultaneously and oleophobic.Here by F13 (CF 3-(CF 2) 5-) and F16 (CF 2H-(CF 2) 7-) silane can obtain significantly useful effect.

Claims (9)

1. a heat exchanger comprises a kind of heat exchanger that has at least one metal surface, especially aluminium or high-quality steel surface, the surface of this heat exchanger has coating, the medium that comprises waste gas impacts this surface, it is characterized in that, described coating comprises a kind of coating material based on nanometer technology.
2. heat exchanger as claimed in claim 1 is characterized in that, described coating comprises a kind of main component of being made up of organic component and inorganic composition.
3. heat exchanger as claimed in claim 1 or 2 is characterized in that described coating comprises silicon.
4. the described heat exchanger of each claim as described above is characterized in that described coating comprises titanium, zirconium, and/or aluminium.
5. the described heat exchanger of each claim as described above is characterized in that described coating comprises magnesium, zinc, and/or calcium.
6. an aforementioned manufacture method that comprises the heat exchanger of exhaust-heat exchanger is characterized in that described coating is made by sol-gel process.
7. manufacture method as claimed in claim 6 is characterized in that at least a colloidal sol is coated on surface to be coated.
8. manufacture method as claimed in claim 7 is characterized in that, described colloidal sol is processed and form a kind of cross-linked polymeric layer.
9. as each described manufacture method in the claim 6 to 8, it is characterized in that, comprise the steps:
A) heat exchanger that will apply is immersed in the coating material, drains then;
B) heat exchanger that has drained is heated in drying oven, and/or a thermal current, particularly thermal air current over-heat-exchanger.
CNA2006800420459A 2005-09-14 2006-09-12 Heat exchanger, in particular exhaust gas heat exchanger Pending CN101305255A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102005043730.3 2005-09-14
DE102005043730A DE102005043730A1 (en) 2005-09-14 2005-09-14 Heat exchanger, in particular exhaust gas heat exchanger

Publications (1)

Publication Number Publication Date
CN101305255A true CN101305255A (en) 2008-11-12

Family

ID=37507708

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2006800420459A Pending CN101305255A (en) 2005-09-14 2006-09-12 Heat exchanger, in particular exhaust gas heat exchanger

Country Status (7)

Country Link
US (1) US20080245512A1 (en)
EP (1) EP1926962A1 (en)
JP (1) JP2009508080A (en)
CN (1) CN101305255A (en)
DE (1) DE102005043730A1 (en)
RU (1) RU2430323C2 (en)
WO (1) WO2007031262A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008033222A1 (en) 2008-07-15 2010-01-21 Behr Gmbh & Co. Kg Producing a part of a heat exchanger comprising aluminum and/or aluminum alloy and having a corrosion protected surface, comprises applying zinc or zinc-containing layer to the surface or part of the surface
DE102008062705A1 (en) 2008-12-18 2010-06-24 Behr Gmbh & Co. Kg Coating method and coating apparatus for manufacturing a component and heat exchangers and use of the heat exchanger
JP5218525B2 (en) * 2010-11-09 2013-06-26 株式会社デンソー Equipment through which heat transport fluid flows
JP5934569B2 (en) * 2012-04-27 2016-06-15 日立Geニュークリア・エナジー株式会社 Heat exchanger with protective member
DE102013215386A1 (en) * 2013-08-05 2015-02-05 Behr Gmbh & Co. Kg Heat exchanger made of aluminum and method for producing a surface coating on a heat exchanger made of aluminum

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DE19813709A1 (en) * 1998-03-27 1999-09-30 Inst Neue Mat Gemein Gmbh Process for protecting a metallic substrate from corrosion
JP2000329497A (en) * 1999-05-19 2000-11-30 Toyobo Co Ltd Fin for heat exchanger in car air conditioner
JP2000329495A (en) * 1999-05-21 2000-11-30 Nissan Motor Co Ltd Heat exchanger for air conditioner and surface treating method therefor
AU1461501A (en) * 1999-12-03 2001-06-12 Caterpillar Inc. Patterned hydrophilic-oleophilic metal oxide coating and method of forming
US6890640B2 (en) * 1999-12-03 2005-05-10 Caterpillar Inc Patterned hydrophilic-oleophilic metal oxide coating and method of forming
JP2001247822A (en) * 2000-03-06 2001-09-14 Kansai Paint Co Ltd Composition and method for treatment for imparting hydrophilic property
DE10045606A1 (en) * 2000-09-15 2002-03-28 Volkswagen Ag Oligodynamic coating for the inner metallic surfaces of automobile air conditioners comprises matrix based on (hetero)-polysiloxanes, nano-scale heavy metal particles and an optional corrosion inhibitor
DE20018520U1 (en) * 2000-10-28 2001-02-01 Pucel Markus Filter-free heat exchangers with nano-technology
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DE102004011544A1 (en) * 2003-03-31 2004-10-14 Behr Gmbh & Co. Kg Heat exchanger for a vehicle comprises a hydrophilic surface coating consisting of a gel produced by a sol-gel method
EP1610911B1 (en) * 2003-03-31 2016-05-11 MAHLE Behr GmbH & Co. KG Heat exchanger and method for treating the surface of said heat exchanger
DE10323729A1 (en) * 2003-05-26 2004-12-16 Institut Für Neue Materialien Gem. Gmbh Composition with non-Newtonian behavior
DE10355833A1 (en) * 2003-11-26 2005-06-23 Behr Gmbh & Co. Kg heat exchangers
DE10359806A1 (en) * 2003-12-19 2005-07-14 Modine Manufacturing Co., Racine Heat exchanger with flat tubes and flat heat exchanger tube
EP1562018A1 (en) * 2004-02-03 2005-08-10 Siemens Aktiengesellschaft Heat exchanger tube, heat exchanger and its use

Also Published As

Publication number Publication date
EP1926962A1 (en) 2008-06-04
RU2430323C2 (en) 2011-09-27
RU2008114316A (en) 2009-10-20
WO2007031262A1 (en) 2007-03-22
JP2009508080A (en) 2009-02-26
US20080245512A1 (en) 2008-10-09
DE102005043730A1 (en) 2007-03-22

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Open date: 20081112