DK200600246Y6 - Mobile pipe drying plant - Google Patents
Mobile pipe drying plant Download PDFInfo
- Publication number
- DK200600246Y6 DK200600246Y6 DK200600246U DKBA200600246U DK200600246Y6 DK 200600246 Y6 DK200600246 Y6 DK 200600246Y6 DK 200600246 U DK200600246 U DK 200600246U DK BA200600246 U DKBA200600246 U DK BA200600246U DK 200600246 Y6 DK200600246 Y6 DK 200600246Y6
- Authority
- DK
- Denmark
- Prior art keywords
- air
- dehumidifier
- cooling
- drying system
- mobile
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/006—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects the gas supply or exhaust being effected through hollow spaces or cores in the materials or objects, e.g. tubes, pipes, bottles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
- F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/12—Velocity of flow; Quantity of flow, e.g. by varying fan speed, by modifying cross flow area
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1032—Desiccant wheel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1068—Rotary wheel comprising one rotor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1088—Rotary wheel comprising three flow rotor segments
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/02—Compressor control
- F25B2600/021—Inverters therefor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/11—Fan speed control
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Gases (AREA)
- Drying Of Solid Materials (AREA)
Description
DK 2006 00246 Y6DK 2006 00246 Y6
BESKRIVELSEDESCRIPTION
BenævnelseDenominations
Mobilt rørtørringsanlæg Frembringelsens anvendelsesområdeMobile pipe drying plant The scope of production
Anlægget anvendes til den indvendige udtørring af hovedsagligt gas-, kemikalie- og olierørledninger, men også til tørring af tanke og beholdere.The plant is used for the internal drying of mainly gas, chemical and oil pipelines, but also for drying tanks and containers.
Det er mobilt på den måde, at det er installeret i en container, som kan flyttes rundt ved hjælp af en lastbil.It is mobile in that it is installed in a container that can be moved around by a truck.
Kendt teknikPrior art
Udtørring af en rørledning foregår i princippet ved at blæse tørret luft igennem rørledningen.Drying of a pipeline is in principle carried out by blowing dried air through the pipeline.
Den tørre luft er frembragt ved at føre atmosfærisk luft igennem først fordamperen (1) på et køleanlæg, hvor luften bliver kølet og den første vandudskilning finder sted. Herefter føres luften igennem en affugter (4), der bla. består af en rotor fremstillet af et stærkt fugtabsorberende materiale, hvor den endelige udtørring og dermed nedbringelsen af luftens dugpunkt til det nødvendige i pkt. D finder sted.The dry air is generated by passing atmospheric air through the first evaporator (1) on a cooling system where the air is cooled and the first water separation takes place. The air is then passed through a dehumidifier (4) which, among other things. consists of a rotor made of a strong moisture-absorbing material, where the final drying out and thus the reduction of the dew point of the air to the required in par. D takes place.
Luften trækkes igennem anlægget ved hjælp af en blæser (5), der også trykker luften op på det tryk, der er nødvendigt for den pågældende rørledning.The air is drawn through the system by means of a fan (5), which also pressures the air up to the pressure required for the relevant pipeline.
Anlægget er installeret i 2 eller flere containere sammen med en generator, der forsyner anlægget med den nødvendige elektriske energi.The system is installed in 2 or more containers together with a generator that supplies the system with the necessary electrical energy.
2 DK 2006 00246 Y62 DK 2006 00246 Y6
Den europæiske patentansøgning EP 0 835 694 a angår et automatiseret luftfiltrerings- og tørringssystem, som anvendes sammen med en sprøjtekabine. Systemet filtrerer den udgående luft fra sprøjtekabinen og sender filtreret og tørret luft tilbage til sprøjtekabinen. Systemet anvender enten et varmebaseret system eller et køleanlæg til tørring af luften. Luft trækkes gennem systemet ved hjælp af en blæser, hvis hastighed styres af en frekvensomformer.European patent application EP 0 835 694 a relates to an automated air filtration and drying system which is used with a spray booth. The system filters the outgoing air from the spray booth and sends filtered and dried air back to the spray booth. The system uses either a heat-based system or a cooling system for drying the air. Air is drawn through the system using a fan whose speed is controlled by a frequency converter.
Den amerikanske patentansøgning US 2005/0086959 Al angår styring af en kompressor ved at variere dens driftsfrekvens.US Patent Application US 2005/0086959 A1 relates to controlling a compressor by varying its operating frequency.
Amerikansk patent US 3,864,102 angår et mobilt system til tørring af rørledninger, og af den art der omfatter en kompressor til at tilføre komprimeret luft fra omgivelserne, en varmeveksler og affugtere.US Patent US 3,864,102 relates to a mobile pipeline drying system, and of the kind comprising a compressor for supplying compressed air from the surroundings, a heat exchanger and dehumidifiers.
Det tekniske problemThe technical problem
De kendte systemer har et begrænset anvendelsesområde pga. begrænsede muligheder for kapacitetsregulering af både blæser samt køleanlæg. Det er afgørende for affugterens effektivitet, at temperaturen på indblæsningsluften på affugteren er stabil og tilstrækkeligt lav.The known systems have a limited scope due to limited possibilities for capacity control of both the fan and the cooling system. It is crucial for the efficiency of the dehumidifier that the temperature of the supply air of the dehumidifier is stable and sufficiently low.
Hvis ikke den aktuelle køleydelse på køleanlægget er tilpasset luftmængden igennem anlægget er det meget vanskeligt at holde en konstant og tilstrækkelig lav lufttemperatur på indblæsningsluften til affugteren uden at fordamperen blokker op med is.Unless the actual cooling performance of the cooling system is adjusted to the air flow through the system, it is very difficult to maintain a constant and sufficiently low air temperature on the supply air to the dehumidifier without the evaporator blocking up with ice.
Det har med frembringelsen været et ønske at konstruere et rørtørringsanlæg med et meget stort anvendelsesområde med hensyn til luftmængden og dermed få muligheden for at kunne anvende anlægget til store såvel som små rørledninger og installationer, uden at gå på kompromis med affugterens 3 DK 2006 00246 Y6 effektivitet. Det er helt afgørende for affugterens funktion og dermed luftens dugpunkt i pkt. D, at temperaturen på luften i pkt. B er stabil og tilstrækkelig lav.With the creation, it has been a desire to design a pipe drying plant with a very large scope in terms of air volume and thus have the opportunity to use the system for large as well as small pipelines and installations, without compromising the dehumidifier's 3 DK 2006 00246 Y6 efficiency. It is absolutely crucial to the dehumidifier's function and thus the dew point of the air in section. D, that the temperature of the air in cl. B is stable and sufficiently low.
Det har desuden været et ønske at konstruere anlægget så kompakt, at én container var tilstrækkelig til hele anlægget inklusiv generator.In addition, it has been a desire to design the plant so compactly that one container was sufficient for the entire plant including generator.
Tidligere anlæg med samme kapacitet soro frembringelsens kapacitet ville kræve to containere, som ved rørtørringsarbejde skulle kobles sammen med luftslanger og elkabler.Previous plants with the same capacity soro production capacity would require two containers, which in connection with pipe drying work had to be connected to air hoses and power cables.
Den nve teknikThe nve technique
Det nye ved frembringelsen er, at der er anvendt frekvensomformere til regulering af luftmængden og til regulering af kompressorydelsen.What is new about the generation is that frequency inverters have been used to control the airflow and to regulate the compressor performance.
Der er ved frembringelsen konstrueret et komplet anlæg i én container, der i dette tilfælde trinløst kan variere den leverede luftmængde fra 2000 mVtime til 6000 m3/time samtidig med at kravet til en stabil og tilstrækkelig lav temperatur i pkt. B tilgodeses under alle forhold, hvilket sikrer det krævede dugpunkt i pkt. dIn the production, a complete system is constructed in one container, which in this case can infinitely vary the delivered air flow from 2000 mVh to 6000 m3 / h while at the same time the requirement for a stable and sufficiently low temperature in par. B is met in all conditions, which ensures the required dew point in section. d
Den tekniske virkningThe technical impact
Den luft, der skal anvendes til udtørringen af rørledningen tages direkte fra omgivelserne og tilgår anlægget i pkt. A. Fra pkt. A til b nedkøles luften ved hjælp af fordamperen (1).The air to be used for desiccation of the pipeline is taken directly from the surroundings and is supplied to the plant in item. A. From paragraph. A to b the air is cooled by means of the evaporator (1).
Overfladetemperaturen på fordamperen skal ligge på cirka -2,0eC. Luften nedkøles fra den omgivende temperatur til cirka +2,0°C. Fra pkt. B tilgår luften affugteren (4), hvor den endelige affugtning finder sted ved hjælp af et fugtabsorberende stof. Fra pkt- C strømmer luften til DK 2006 00246 Y6 Λ indsugningen på blæseren (6) og trykkes her videre til pkt. □, hvorfra luften tilgår den rørledning, der skal tørres. Luftmængden afhænger af rørledningens dimension og kan justeres meget nøjagtigt med blæserens frekvensomformer.The surface temperature of the evaporator should be around -2.0 ° C. The air is cooled from the ambient temperature to about + 2.0 ° C. From point. B enters the air dehumidifier (4), where the final dehumidification takes place by means of a moisture-absorbing substance. From point-C the air flows to the DK 2006 00246 Y6 Λ suction on the fan (6) and is then pushed on to point. □ from which the air enters the pipeline to be dried. The amount of air depends on the dimension of the pipeline and can be adjusted very precisely with the fan frequency converter.
ved en reduktion af luftmængden reduceres belastningen på køleanlægget dog også- Ved uændret omdrejningshastighed ville overfladetemperaturen på fordamperen {l) falde hvilket kan føre til en opblokning af fordamperen med is.however, by reducing the amount of air, the load on the refrigeration system is also reduced.
Ved en forøgelse af luftmængden forøges belastningen på køleanlægget. ved uændret omdrejningshastighed ville overfladetemperaturen på fordamperen (1) stige hvilket ville reducere affugterens (4) effektivitet.By increasing the amount of air, the load on the cooling system increases. at unchanged speed the surface temperature of the evaporator (1) would increase which would reduce the efficiency of the dehumidifier (4).
Ved hjælp af kølekompressorens (3) frekvensomformer tilpasses køleydelsen og dermed overfladetemperaturen på fordamperen dog konstant til den aktuelle luftmængde, og dermed forhindres driftsstop pga. opblokning med is. Desuden sikres fuld effektivitet på affugteren.However, with the help of the refrigeration compressor (3) frequency converter, the cooling performance and thus the surface temperature of the evaporator are constantly adjusted to the current air volume, thus preventing shutdowns due to ice blockage. Furthermore, full efficiency on the dehumidifier is ensured.
FicrurfortecmelseFicrurfortecmelse
Figur 1 viser en principskitse af den nye frembringelse, hvor de forskellige komponenter som luften møder fra pkt, A til p er anført.Figure 1 shows a principle sketch of the new generation, where the various components that the air meets from points A to P are listed.
UdførelseseksempelEmbodiment
Under henvisning til figur 1 følger hermed et principielt eksempel på en udførelse.Referring now to Figure 1, here is a basic example of an embodiment.
Anlægget er udført med et køleanlæg, en affugter (4) og en blæser (5).The system is equipped with a cooling system, a dehumidifier (4) and a fan (5).
Det hele er forsynet elektrisk fra en dieselgenerator (7).The whole is electrically supplied from a diesel generator (7).
5 DK 2006 00246 Y65 DK 2006 00246 Y6
Atmosfærisk luft tilgår anlægget i pkt. A. Fra pkt. A til pkt. B bliver luften kølet ved hjælp af køleanlæggets fordamper (1).Atmospheric air is available to the system in item. A. From paragraph. A to par. B, the air is cooled by the evaporator (1) of the cooling system.
Fordampningstemperaturen holdes på -1,0 til -2,0°C. Fordampningstemperaturen reguleres af frekvensomformeren (2), der konstant tilpasser kølekompressorens (3) omdrejningshastighed til den aktuelle belastning på fordamperen. Belastningen afhænger af den aktuelle luftmængde samt den aktuelle temperatur og relative fugtighed på den atmosfæriske luft i pkt. a.The evaporation temperature is maintained at -1.0 to -2.0 ° C. The evaporation temperature is controlled by the frequency converter (2), which constantly adjusts the speed of the cooling compressor (3) to the current load on the evaporator. The load depends on the current airflow as well as the current temperature and relative humidity of the atmospheric air in section. a.
Fordampningstemperaturen tilpasses den aktuelle belastning således, at lufttemperaturen i pkt- B ligger på +2,00°C.The evaporation temperature is adjusted to the current load so that the air temperature in point B is + 2.00 ° C.
Fra pkt. B til C affugtes luften i affugteren (4).From point. B to C dehumidify the air in the dehumidifier (4).
Affugteren består af en procesluftblæser, som sender luften fra pkt. b igennem en rotor inde i affugteren, der er fremstillet af et stærkt fugtabsorberende materiale, internt i affugteren er der også et system for regenerering af rotoren. Opvarmet regenereringsluft sendes af en anden intern blæser igennem en del af den konstant roterende rotor, hvorved rotoren regenereres.The dehumidifier consists of a process air blower which sends the air from section. b through a rotor inside the dehumidifier made of a strong moisture absorbing material, internally within the dehumidifier there is also a system for regenerating the rotor. Heated regeneration air is sent by another internal blower through a portion of the constantly rotating rotor, thereby regenerating the rotor.
Den tørre luft forlader affugteren i pkt. C, hvor luften tilgår blæseren (6), I denne udførelse er blæseren en kapselblæser.The dry air leaves the dehumidifier in cl. C, where the air enters the fan (6). In this embodiment, the fan is a capsule fan.
I pkt. D forlader den tørre luft anlægget, og sendes via slanger fra containeren til den installation, som skal tørres. I mange tilfælde vil det være gas- og olierørledninger.In cl. D leaves the dry air system and is sent via hoses from the container to the installation to be dried. In many cases it will be gas and oil pipelines.
Trykstigningen fra pkt. C til D afhænger af dimensionerne på den pågældende rørledning.The increase in pressure from p. C to D depend on the dimensions of the relevant pipeline.
DK 2006 00246 Y6 6DK 2006 00246 Y6 6
Luftmængden afhænger også af dimensionerne på den pågældende rørledning. Ved hjælp af frekvensomformeren (5) tilpasses blæserens omdrejningshastighed nøjagtigt til den aktuelle rørledning.The amount of air also depends on the dimensions of the particular pipeline. Using the frequency converter (5), the fan speed of rotation is exactly matched to the current pipeline.
Generatoren (7) leverer den nødvendige elektriske energi til anlægskomponenteme.The generator (7) supplies the necessary electrical energy to the plant components.
Claims (10)
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK200600246U DK200600246Y6 (en) | 2006-09-19 | 2006-09-19 | Mobile pipe drying plant |
DK07826457.9T DK2100084T3 (en) | 2006-09-19 | 2007-09-19 | A dryer for drying a pipeline and a method for using the apparatus |
PCT/IB2007/053800 WO2008035298A2 (en) | 2006-09-19 | 2007-09-19 | A drying apparatus for drying a hollow object and a method of using the apparatus |
EP07826457.9A EP2100084B1 (en) | 2006-09-19 | 2007-09-19 | A drying apparatus for drying a pipeline and a method of using the apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK200600246U DK200600246Y6 (en) | 2006-09-19 | 2006-09-19 | Mobile pipe drying plant |
Publications (2)
Publication Number | Publication Date |
---|---|
DK200600246U3 DK200600246U3 (en) | 2006-10-27 |
DK200600246Y6 true DK200600246Y6 (en) | 2007-10-12 |
Family
ID=37189904
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK200600246U DK200600246Y6 (en) | 2006-09-19 | 2006-09-19 | Mobile pipe drying plant |
DK07826457.9T DK2100084T3 (en) | 2006-09-19 | 2007-09-19 | A dryer for drying a pipeline and a method for using the apparatus |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK07826457.9T DK2100084T3 (en) | 2006-09-19 | 2007-09-19 | A dryer for drying a pipeline and a method for using the apparatus |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2100084B1 (en) |
DK (2) | DK200600246Y6 (en) |
WO (1) | WO2008035298A2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT514801B1 (en) * | 2013-11-22 | 2015-04-15 | Heutrocknung Sr Gmbh | Method for drying of drying material |
CN114111310B (en) * | 2021-11-30 | 2023-01-03 | 江苏西铭节能环保科技有限公司 | Inside drying system of batcher is carried to material |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3864102A (en) * | 1973-06-25 | 1975-02-04 | Pipeline Dehydrators Inc | Dehydration of a pipeline with a portable dry air generating plant |
IL64915A (en) * | 1982-02-02 | 1985-04-30 | Joel Harband | Apparatus and method for temperature and humidity control |
DE68928556T2 (en) * | 1988-11-02 | 1998-04-30 | Colortronic Co | Air dryer with adsorbent |
DE4317768A1 (en) * | 1993-05-28 | 1994-12-01 | Somos Gmbh | Method and device for processing a particularly moist adsorbent |
DE9316950U1 (en) * | 1993-11-05 | 1994-01-05 | Munters Gmbh | Device for the continuous dehumidification of moist air |
SE502635C2 (en) * | 1995-01-10 | 1995-11-27 | Corroventa Avfuktning Ab | Methods and plant to increase the yield of an air drying process |
SG83158A1 (en) * | 1998-12-12 | 2001-09-18 | Univ Singapore | A modular heat pump system for drying and air-conditioning |
US6094835A (en) * | 1998-12-14 | 2000-08-01 | University Of Central Florida | Heat pump dryer with desciccant enhanced moisture removal |
US6711907B2 (en) * | 2001-02-28 | 2004-03-30 | Munters Corporation | Desiccant refrigerant dehumidifier systems |
JP4775623B2 (en) * | 2004-10-26 | 2011-09-21 | 株式会社日立プラントテクノロジー | Dehumidification system |
DE202004018635U1 (en) * | 2004-12-01 | 2005-03-24 | Weigel Klaus | Mobile grain drier for field use is mounted in a separate trailer with integral power source to process granular products using a swirl effect channel and with warmed and cooled air flows |
-
2006
- 2006-09-19 DK DK200600246U patent/DK200600246Y6/en not_active IP Right Cessation
-
2007
- 2007-09-19 DK DK07826457.9T patent/DK2100084T3/en active
- 2007-09-19 WO PCT/IB2007/053800 patent/WO2008035298A2/en active Application Filing
- 2007-09-19 EP EP07826457.9A patent/EP2100084B1/en not_active Not-in-force
Also Published As
Publication number | Publication date |
---|---|
EP2100084A2 (en) | 2009-09-16 |
EP2100084B1 (en) | 2014-12-10 |
WO2008035298A2 (en) | 2008-03-27 |
DK2100084T3 (en) | 2015-03-09 |
DK200600246U3 (en) | 2006-10-27 |
WO2008035298A9 (en) | 2009-03-19 |
WO2008035298A3 (en) | 2009-01-29 |
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UUP | Utility model expired |
Expiry date: 20160919 |