CN207632748U - A kind of White Mineral Oil special production apparatus of classification removal micro-moisture - Google Patents
A kind of White Mineral Oil special production apparatus of classification removal micro-moisture Download PDFInfo
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- CN207632748U CN207632748U CN201721779602.7U CN201721779602U CN207632748U CN 207632748 U CN207632748 U CN 207632748U CN 201721779602 U CN201721779602 U CN 201721779602U CN 207632748 U CN207632748 U CN 207632748U
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- moisture
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- mineral oil
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Abstract
The utility model discloses a kind of White Mineral Oil special production apparatus of classification removal micro-moisture.The device includes by the sequentially connected Mixer pot of pipeline, first step drier, hypergravity de-watering apparatus, first step drier is deflector type fixed bed drying device, inside set the first filler, second filler is set in hypergravity de-watering apparatus, the design of deflector type filler can increase the contact area of material in drier, just water rem oval be improved, then through hypergravity equipment, micro-moisture is removed, with the entire removal process of batches about 5min.In the fixed bed drying device of the first step, the water content of processed oil product is less than 40ppm, meet basic oil product water removal to require, this is walked out of oil and removes more micro moisture through hypergravity equipment, the water content of oil product is 10 25ppm, can be applied to catalyst industry, whole device is small, conveniently moving, it is efficient.
Description
Technical field
The utility model is related to a kind of White Mineral Oil special production apparatus more particularly to a kind of classification to remove the white of micro-moisture
Dormant oil special production apparatus belongs to Petrochemical Production Technologies field.
Background technology
In White Mineral Oil production process, there is no special requirements to moisture for the White Mineral Oil or White Mineral Oil of general applications.But
Be in the field of particular/special requirement, as transformer oil production in, it is desirable that oil in water content be no more than 70ppm, it is fine in winter
It is produced under bright weather condition, production requirement can be reached, but in the case that southern air humidity is relatively high, without water removal
Equipment, oil product cannot be satisfied requirement.The dedicated White Mineral Oil of catalyst, moisture requirement is no more than 25ppm, in common production technology
Under, requirement is cannot be satisfied, therefore can generally be removed water by heating.But only heating water removal in current water removal device, can only will be oily
Free water and floating water in product remove, and fat liquor system is even formd for the micro moisture being dispersed in oil
Moisture, it is more difficult to remove.Water removal device relatively advanced at present, is filtered using clay, adsorbs micro-moisture.The technology and device
Defect be：Water removal is unable to reach lower level most down to 35ppm；Batch production removes water time about 20- every time
40min；Equipment occupation space is larger, and water-absorbent material is single, and carclazyte needs replacement processing repeatedly, Reusability less efficient；
And pre-treatment needs to heat and can be only achieved water removal purpose, and whole efficiency is low, and energy consumption is high, and micro-moisture can not remove.Excessively add
Heat can cause White Mineral Oil to turn yellow, to which product is rotten.
The utility model uses multistep treatment, using deflector type fixed bed drying device, connects hypergravity de-watering apparatus, at different levels
Using different fillers, whole device is small, and conveniently moving, heating time is short, and sectional removes moisture, to meet different product
Requirement, low power consuming, high efficiency, can will water removal the time foreshorten to 5min.
Utility model content
The purpose of this utility model is that generally requiring heating for existing water removal device could remove water, and remove water the time
The defects of length, energy consumption is high, while micro moisture can not remove provides a kind of special life of White Mineral Oil of classification removal micro-moisture
Produce device.The device uses baffling using fixed bed drying device and the cooperation classification water removal of hypergravity equipment especially in drier
Formula filler designs, and increases the contact area of material, improves just water rem oval, then through hypergravity equipment, removes micro-moisture, together
The entire removal process of batches about 5min.In the fixed bed drying device of the first step, the water content of processed oil product is less than
40ppm meets basic oil product water removal and requires, this is walked out of oil and removes more micro moisture through hypergravity equipment, and oil product contains
Water is 10-25ppm, can be applied to catalyst industry, subsequently canned through whole process sealing, ensures oil quality.
The White Mineral Oil special production apparatus of the classification removal micro-moisture of the utility model, including be sequentially connected by pipeline
Mixer pot, first step drier, hypergravity de-watering apparatus and the pump being used to provide power；The first step drier is
Deflector type fixed bed drying device, it is internal to use Multi-level deflector formula pipeline, it is equipped with the first filler in deflector type pipeline, hypergravity removes
Second filler is set in water installations, in the connecting pipe of Mixer pot and deflector type fixed bed drying device, deflector type fixed bed drying
It is equipped with the oil outlet controlled by valve in the connecting pipe of device and hypergravity de-watering apparatus.
First filler is anhydrous calcium chloride, anhydrous magnesium chloride, silica gel, atlapulgite, A type molecular sieve or X-type point
Son sieve.
Second filler is A type molecular sieve, Y type molecular sieve or X-type molecular sieve.
The device of the utility model then may be used to the product of moisture no requirement (NR) in use, White Mineral Oil first passes through Mixer pot reconciliation
Directly to become finished product by canned by Mixer pot oil outlet.There is the product of strict demand then to enter the first step moisture to dry
Device, deflector type fixed bed drying device, oil product carry out comprehensive engagement in drier, by deflector type and filler, are provided by pump dynamic
Power carries out primary dry water removal by fixed bed drying device, and whole process does not cause to damage without heating equipment to oil quality.
Water removal can make the water content of oil product be down to 30-45ppm herein, if desired can be directly canned at this by the oil outlet of drier
The finished product of grade.In requirement higher of the catalyst industry to White Mineral Oil product, need to use more accurate micro water removal
Equipment, therefore oil product need to enter super-gravity device, under the high speed rotation of super-gravity device, oil product is dispersed into minimum list
Position, respectively by filler, micro-moisture is spread out at this time, is adsorbed when passing through filler, to cause denier moisture and
White Mineral Oil separates, and molecular sieve filling is used in hypergravity de-watering apparatus, molecular sieve is utilized to White Mineral Oil without adsorption energy
The property of power.Entire separation process about 3min, and super-gravity device can continue working, ensure that the efficient of separation, precisely.
The product detached herein can reach 10-25ppm, meet catalyst industry or to the more stringent row of White Mineral Oil moisture requirement
The demand of industry, subsequently canned to need whole process closed canned, reduction is contacted with air, and moisture in air is avoided to enter White Mineral Oil product
In.
The utility model has the beneficial effects that：
1. by hypergravity equipment application to dewatering process, water rem oval is improved, shortens material (grease) disengaging time, together
When micro-moisture can be separated.
2. fixed bed drying device uses deflector type filler, the comprehensive engagement of material, water rem oval higher, liquid flow ensure that
Dynamic speed is faster.
3. entire water removal device high-efficiency operation, removal process about 5min can be completed, and reduce the influence to White Mineral Oil quality.
4. can according to water removal require, carry out classification water removal it is canned, grading is clear.
5. the occupied space of whole device is smaller, space is greatly saved, while the mobility of equipment is strong, it can be to difference
White Mineral Oil product and there are other White Mineral Oil products of particular/special requirement to carry out water removal and accurate micro water removal.
Description of the drawings
Fig. 1 is the structural schematic diagram of utility model device.
Specific implementation mode
Referring to Fig.1, the White Mineral Oil special production apparatus of the classification removal micro-moisture of the utility model, including pass through pipeline
The trend of sequentially connected Mixer pot, first step drier, hypergravity de-watering apparatus, White Mineral Oil provides power by pump；Described
First step drier is deflector type fixed bed drying device, internal to use Multi-level deflector formula pipeline, and the is equipped in deflector type pipeline
One filler, the first filler are anhydrous calcium chloride, anhydrous magnesium chloride, silica gel, atlapulgite, A type molecular sieve or X-type molecular sieve.It is super
Second filler is set in gravity de-watering apparatus, and the second filler uses A type molecular sieve, Y type molecular sieve or X-type molecular sieve.It is reconciling
The connecting pipe of tank and deflector type fixed bed drying device, the connecting pipe of deflector type fixed bed drying device and hypergravity de-watering apparatus
On be equipped with the oil outlet controlled by valve.The device such as CN206082411U may be used in the Mixer pot of the present invention, through reconciling
Afterwards, directly canned to the product of moisture no requirement (NR) is finished product.The product finely removed water is needed, enters fixed bed deflector type through pipeline
Drier, through repeatedly reverse-flow type water removal after, reach moisture requirement, to moisture requirement grade in 30-50ppm can be straight
Cans picking dresses up finished product.The follow-up removing for needing denier moisture, oil product enter hypergravity de-watering apparatus through pipeline, are revolved through high speed
Turning, oil product is dispersed into nano sized particles, is more easy to make packing material absorbing moisture, after water-oil separating, the leakage fluid dram separation below product device
Out, whole sealing is canned after pipeline.Obtain the oil product of water content 10-25ppm.
Claims (3)
1. a kind of White Mineral Oil special production apparatus of classification removal micro-moisture, which is characterized in that including being connected successively by pipeline
Mixer pot, first step drier, hypergravity de-watering apparatus and the pump being used to provide power connect；The first step drier
It is internal to use deflector type pipeline for deflector type fixed bed drying device, the first filler, hypergravity water removal are equipped in deflector type pipeline
Second filler is set in device, in the connecting pipe of Mixer pot and deflector type fixed bed drying device, deflector type fixed bed drying device
And the oil outlet controlled by valve is equipped in the connecting pipe of hypergravity de-watering apparatus.
2. the White Mineral Oil special production apparatus of classification removal micro-moisture according to claim 1, which is characterized in that described
The first filler be anhydrous calcium chloride, anhydrous magnesium chloride, silica gel, atlapulgite, A type molecular sieve or X-type molecular sieve.
3. the White Mineral Oil special production apparatus of classification removal micro-moisture according to claim 1, which is characterized in that described
The second filler be A type molecular sieve, Y type molecular sieve or X-type molecular sieve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721779602.7U CN207632748U (en) | 2017-12-19 | 2017-12-19 | A kind of White Mineral Oil special production apparatus of classification removal micro-moisture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721779602.7U CN207632748U (en) | 2017-12-19 | 2017-12-19 | A kind of White Mineral Oil special production apparatus of classification removal micro-moisture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207632748U true CN207632748U (en) | 2018-07-20 |
Family
ID=62852261
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721779602.7U Expired - Fee Related CN207632748U (en) | 2017-12-19 | 2017-12-19 | A kind of White Mineral Oil special production apparatus of classification removal micro-moisture |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207632748U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109308961A (en) * | 2018-11-24 | 2019-02-05 | 运城清海科技有限公司 | A kind of transformer dry equipment |
| CN109692503A (en) * | 2019-01-24 | 2019-04-30 | 湖南昊华化工有限责任公司 | A kind of device and method removing minim moisture from organic solvent |
-
2017
- 2017-12-19 CN CN201721779602.7U patent/CN207632748U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109308961A (en) * | 2018-11-24 | 2019-02-05 | 运城清海科技有限公司 | A kind of transformer dry equipment |
| CN109308961B (en) * | 2018-11-24 | 2024-03-08 | 运城清海科技有限公司 | Transformer drying equipment |
| CN109692503A (en) * | 2019-01-24 | 2019-04-30 | 湖南昊华化工有限责任公司 | A kind of device and method removing minim moisture from organic solvent |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180720 Termination date: 20191219 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |