CN103695150A - Regeneration technology of transformer insulating oil - Google Patents

Regeneration technology of transformer insulating oil Download PDF

Info

Publication number
CN103695150A
CN103695150A CN201310725416.5A CN201310725416A CN103695150A CN 103695150 A CN103695150 A CN 103695150A CN 201310725416 A CN201310725416 A CN 201310725416A CN 103695150 A CN103695150 A CN 103695150A
Authority
CN
China
Prior art keywords
transformer
oil
storage tank
insulation
reclaiming process
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
CN201310725416.5A
Other languages
Chinese (zh)
Inventor
张新建
高纪立
孟朝锋
闫林华
董朝辉
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.)
ZHENGZHOU RONGQI THERMOELECTRICITY ENERGY CO Ltd
Original Assignee
ZHENGZHOU RONGQI THERMOELECTRICITY ENERGY CO Ltd
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 ZHENGZHOU RONGQI THERMOELECTRICITY ENERGY CO Ltd filed Critical ZHENGZHOU RONGQI THERMOELECTRICITY ENERGY CO Ltd
Priority to CN201310725416.5A priority Critical patent/CN103695150A/en
Publication of CN103695150A publication Critical patent/CN103695150A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Transformer Cooling (AREA)

Abstract

The invention belongs to the technical field of regeneration of oils, and particularly relates to a regeneration technology of transformer insulating oil. The transformer insulating oil adopts the open circulation; meanwhile, the atmospheric pressure around the insulating oil is reduced. In conclusion, the regeneration technology of the insulating oil improves the regeneration efficiency of the insulating oil, largely enhances the quality of the insulating oil, and has strong practical and promotional values.

Description

A kind of reclaiming process of transformer insulation oil
Technical field
The invention belongs to oils regeneration techniques field, particularly a kind of reclaiming process of transformer insulation oil.
Background technology
Transformer is important electric installation, and transformer insulation oil is the important insulation of transformer and heat-eliminating medium, and the quality of transformer oil directly affects the safe and stable operation of transformer.Transformer insulation oil is in long-term operational process, be subject to the effect of electric field, humidity, temperature, light, oxygen and foreign material, its chemical physics performance and dielectric properties progressively degenerate and are aging, the result that transformer oil is aging will produce the suspended substances such as various oxide compounds, moisture, organic acid, methane, ethene, acetylene, carbon granules, cause transformer oil variable color, acid number rising, flash-point to reduce, dielectric properties worsen.The fault of some transformers and accident have direct relation with the quality of transformer oil invariably.At present, the regeneration of transformer insulation oil is all to adopt closed cycle to filter, and transformer insulation oil enters oil filter from the bottom of transformer, and then from oil filter outlet, enters the top of transformer, because transformer oil is mixing in filtration procedure always, so oil strain efficiency is relatively low.Special in the large user of transformer consumption, as power plant etc., transformer insulated oilreserves is large, if according to current regeneration purification techniques, the regeneration of transformer insulation oil is for time-consuming a, effort, inefficient loaded down with trivial details work.How to shorten oil filtration time, improve oil strain efficiency and become the problem that transformer insulation oil reclaiming process important solution.
Summary of the invention
The reclaiming process that the object of this invention is to provide a kind of transformer insulation oil, can overcome that current technique is time-consuming, effort, inefficient problem.
For solving the problems of the technologies described above, the technical solution used in the present invention is as follows:
A reclaiming process for transformer insulation oil, described transformer insulation oil adopts open cycle, reduces transformer oil air pressure around simultaneously.
Described open cycle is preferably as follows to be carried out: the transformer oil in transformer enters storage tank after filtering by oil filter, all enters after storage tank, then the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration until transformer oil.
Preferably, when the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration, start vacuum pumping pump, in transformer-cabinet, keep vacuum.Now keep vacuum, just can oil downwards " spray " disperse and form film while coming, and be sprayed at oil in device body from the top down in mobile process, oil meter area increases, fully be exposed to certain hour in vacuum, in oil, through the de-not most gas of two-stage vacuum oil filter, moisture, volatile acid etc., by vacuum pump, extracted out.
Further, the transformer oil in transformer enters in the process of storage tank after filtering by oil filter, when in transformer, transformer oil is lower than transformer-cabinet top 2cm, starts transformer to vacuumize.The time specifically vacuumizing takes out less than oil when vacuumizing.
Vacuum keep is 60-70pa.Concrete, the large I of vacuum tightness is adjusted according to the specification of transformer, as long as keep certain vacuum tightness.
When the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration, when the transformer oil height in transformer floods transformer core 2-3cm, detect transformer oil and whether reach standards for recycling; If not up to standard, repeat transformer oil and enter storage tank through strainer, then enter the process of transformer until transformer oil meets standards for recycling by storage tank secondary filtration.
The temperature of transformer oil is controlled as 60-70 ℃.
The flow of transformer oil is 2000-3500L/h.Continuous vacuumizing in degasification process, for improving degassing efficiency, also for reducing the impact of oil stream to core insulation, flow is preferably controlled simultaneously.Flow can suitably be adjusted according to the vacuum tightness in the size of transformer and transformer.
Oil filter adopts two-stage vacuum oil filter.
The present invention changes traditional closed cycle into open cycle, while avoided transformer oil to filter the problem of mixing.In addition, through research, transformer insulated oil gas dissolubility except with the characteristic of gas, outside the Pass the chemical composition of oil has, also humidity, the ambient air pressure when dissolving has close relationship.Under comparatively high temps and subatmospheric, in oil, dissolved gases moisture easily overflows from oil.Therefore but too high temperature easily makes transformer oil aging, reduce gas and moisture that transformer oil air pressure around can reduce dissolved in insulating oil, so that the small molecule hydrocarbon in oil, hydrogen, moisture, carbonic acid gas overflow.
On supporting equipment, except using two-stage vacuum oil filter and storage tank, transformer, on transformer body, increase and connect an evacuator.
Technique of the present invention has guaranteed degassing efficiency on the one hand, also has on the other hand dehydration concurrently and drives damp function.In the transformer box shell of high vacuum, oil downwards " spray " disperse and form film while coming, and be sprayed at oil in device body from the top down in mobile process, oil meter area increases, fully be exposed to certain hour in vacuum, in oil, through the de-not most gas of two-stage vacuum oil filter, moisture, volatile acid etc., by vacuum pump, extracted out, in addition because oily heat conductivity is good, the thermal capacity of oil is large again, and device body is played to deep fat heat drying effect to a certain extent.
By the improvement to transformer insulation oil oil strain technological process, transformer oil regeneration efficiency and quality have been improved, shortened oil strain process time, oil filtration time is shortened more than 20 times, thereby the transformer overhaul duration is shortened greatly, reduced the power consumption of oil filter, reduced the expenditure of time of filtering oil for transformer work, alleviate maintainer's work load, for the safe operation of equipment, established solid basis, there is good technical prospect and promotional value.
To sum up, transformer oil reclaiming process of the present invention has not only improved the regeneration efficiency of transformer oil, has also greatly improved the quality of transformer oil, has very strong practical and popularizing value.
Accompanying drawing explanation
Fig. 1 is that the present invention carries out back and forth the schema of one direction vacuum outgas between storage tank and transformer body by transformer body.
Embodiment
With specific embodiment, technical scheme of the present invention is described below, but protection scope of the present invention is not limited to this:
A reclaiming process for transformer insulation oil, described transformer insulation oil adopts open cycle, reduces transformer oil air pressure around simultaneously.
Transformer oil in transformer enters storage tank after filtering by oil filter, all enters after storage tank, then the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration until transformer oil.
Referring to Fig. 1, in figure, dotted line represents that oil flows to storage tank from transformer, and solid line represents that in degasification process, oil flows to transformer from storage tank.Transformer oil in transformer enters in the process of storage tank after filtering by oil filter, in transformer transformer oil lower than transformer-cabinet top 2cm( transformer oil is not extracted out and to be as the criterion) time, starting transformer to be evacuated to vacuum tightness is 66.66pa; When the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration, when the transformer oil height in transformer floods transformer core 2-3cm, detect transformer oil and whether reach standards for recycling; If not up to standard, repeat transformer oil and enter storage tank through strainer, then enter the process of transformer oil until transformer oil meets standards for recycling by storage tank secondary filtration.The temperature of transformer oil is controlled as 60-70 ℃, and the flow of transformer oil is 3500L/h.
Oil filter adopts two-stage vacuum oil filter.
30 tons of transformer insulation oils are carried out to stratographic analysis, then through 20 hours (by minimum need of traditional technology 15 days) two single loops, (single loop refers to after the transformer oil in transformer filters by oil filter and enters storage tank, until transformer oil, all enter after storage tank, again the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration) regeneration, again transformer oil is carried out to stratographic analysis afterwards, analytical results is as shown in table 1:
Table 1
? Before regeneration After regeneration
H 2(uL/L) 217 0.64
CO 2(uL/L) 4729 192
CO(uL/L) 743 1
Total hydrocarbon (uL/L) 66 0.95
Visible, transformer insulation oil utilizes the present embodiment renovation process to reach new oil standard, and has greatly shortened the recovery time.

Claims (9)

1. a reclaiming process for transformer insulation oil, is characterized in that, described transformer insulation oil adopts open cycle, reduces transformer oil air pressure around simultaneously.
2. the reclaiming process of transformer insulation oil as claimed in claim 1, it is characterized in that, transformer oil in transformer enters storage tank after filtering by oil filter, all enters after storage tank, then the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration until transformer oil.
3. the reclaiming process of transformer insulation oil as claimed in claim 2, is characterized in that, when the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration, keeps vacuum in transformer-cabinet.
4. the reclaiming process of transformer insulation oil as claimed in claim 3, it is characterized in that, transformer oil in transformer enters in the process of storage tank after filtering by oil filter, when in transformer, transformer oil is lower than transformer-cabinet top 2cm, starts transformer to vacuumize.
5. the reclaiming process of transformer insulation oil as claimed in claim 4, is characterized in that, vacuum keep is 60-70pa.
6. the reclaiming process of transformer insulation oil as claimed in claim 3, it is characterized in that, when the transformer oil in storage tank is entered to transformer after by oil filter secondary filtration, when the transformer oil height in transformer floods transformer core 2-3cm, detect transformer oil and whether reach standards for recycling; If not up to standard, repeat transformer oil and enter storage tank through strainer, then enter the process of transformer until transformer oil meets standards for recycling by storage tank secondary filtration.
7. the reclaiming process of the transformer insulation oil as described in as arbitrary in claim 1-6, is characterized in that, the temperature of transformer oil is controlled as 60-70 ℃.
8. the reclaiming process of transformer insulation oil as claimed in claim 7, is characterized in that, the flow of transformer oil is 2000-3500L/h.
9. the reclaiming process of transformer insulation oil as claimed in claim 7, is characterized in that, oil filter adopts two-stage vacuum oil filter.
CN201310725416.5A 2013-12-25 2013-12-25 Regeneration technology of transformer insulating oil Pending CN103695150A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310725416.5A CN103695150A (en) 2013-12-25 2013-12-25 Regeneration technology of transformer insulating oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310725416.5A CN103695150A (en) 2013-12-25 2013-12-25 Regeneration technology of transformer insulating oil

Publications (1)

Publication Number Publication Date
CN103695150A true CN103695150A (en) 2014-04-02

Family

ID=50356819

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310725416.5A Pending CN103695150A (en) 2013-12-25 2013-12-25 Regeneration technology of transformer insulating oil

Country Status (1)

Country Link
CN (1) CN103695150A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104157407A (en) * 2014-08-27 2014-11-19 国家电网公司 Device for handling water or gas with content exceeding standards in oil of oil-immersed transformer

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012114309A1 (en) * 2011-02-25 2012-08-30 Sabic Innovative Plastics Ip B.V. Thermally conductive and electrically insulative polymer compositions containing a low thermally conductive filler and uses thereof
CN203338910U (en) * 2013-06-03 2013-12-11 郑州荣奇热电能源有限公司 Insulating oil regenerative device of transformer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012114309A1 (en) * 2011-02-25 2012-08-30 Sabic Innovative Plastics Ip B.V. Thermally conductive and electrically insulative polymer compositions containing a low thermally conductive filler and uses thereof
CN203338910U (en) * 2013-06-03 2013-12-11 郑州荣奇热电能源有限公司 Insulating oil regenerative device of transformer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104157407A (en) * 2014-08-27 2014-11-19 国家电网公司 Device for handling water or gas with content exceeding standards in oil of oil-immersed transformer

Similar Documents

Publication Publication Date Title
CN105771559B (en) A kind of carbon dioxide capture device and method suitable for before coal gasification combustion
CN203116443U (en) Drying device for lithium iron battery cell
CN101822929B (en) Method for capturing carbon dioxide by utilizing electrical desorption technology
CN104163404B (en) Recoverying and utilizing method and the device of dirty oxide gas is regenerated in nitrogen purification process
CN104560254A (en) Freeze-drying, purification and dehydration process of natural gas
CN208932983U (en) A kind of device extracting helium from hydrogeneous raw helium
CN103695150A (en) Regeneration technology of transformer insulating oil
CN111874864B (en) Solar photocatalytic hydrogen production system for safely separating hydrogen
CN203281202U (en) Air drying generator for ultra-high-voltage transformer
CN203338910U (en) Insulating oil regenerative device of transformer
CN203754664U (en) Molecular sieve adsorption device of circularly regenerating natural gas in close manner
CN203284374U (en) Pure integration dehydration device of liquefied hydrocarbon
CN110124443B (en) Organic waste gas recycling device and method
CN104194852A (en) High-yield light hydrocarbon recovery method from low-pressure natural gas
CN103240059A (en) Preparation method of active carbon for oil gas recovery
CN103691257B (en) Glyphosate tail gas absorption liquid utilization process and equipment thereof
CN203678222U (en) Glyphosate tail gas absorption liquid recycling equipment
CN102527186A (en) Technology and system for recycling solvent oil from oil gas of butadiene prepared from butane under oxidative dehydrogenation effect
CN203474459U (en) Nitrogen blowing-drying system
CN104190201A (en) Landfill gas separating and purifying process and device
CN203469814U (en) Regeneration recycling system of decarbonization solution capable of absorbing carbon dioxide
CN205011723U (en) Rely on device of low temperature methanol solution desorption synthetic natural gas normal water
CN203208872U (en) Dry air generator
CN103113945B (en) Marsh gas purification system and marsh gas purification method
CN105289270A (en) Chemical adsorption-based gas phase mercury removal method and special-purpose apparatus

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20140402

RJ01 Rejection of invention patent application after publication