CN108722981A - A kind of method of paraffin in quick removing dewatering box - Google Patents
A kind of method of paraffin in quick removing dewatering box Download PDFInfo
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- CN108722981A CN108722981A CN201810357992.1A CN201810357992A CN108722981A CN 108722981 A CN108722981 A CN 108722981A CN 201810357992 A CN201810357992 A CN 201810357992A CN 108722981 A CN108722981 A CN 108722981A
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- dewatering box
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- 239000012188 paraffin wax Substances 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 15
- 238000010494 dissociation reaction Methods 0.000 claims abstract description 13
- 230000005593 dissociations Effects 0.000 claims abstract description 13
- 238000007654 immersion Methods 0.000 claims abstract description 12
- 235000019441 ethanol Nutrition 0.000 claims abstract description 11
- 238000009396 hybridization Methods 0.000 claims abstract description 11
- 238000011065 in-situ storage Methods 0.000 claims abstract description 11
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 11
- 229920002545 silicone oil Polymers 0.000 claims abstract description 11
- LPEKGGXMPWTOCB-GSVOUGTGSA-N methyl (R)-lactate Chemical class COC(=O)[C@@H](C)O LPEKGGXMPWTOCB-GSVOUGTGSA-N 0.000 claims abstract description 7
- 238000011017 operating method Methods 0.000 claims abstract description 7
- 230000008569 process Effects 0.000 claims abstract description 7
- JPAOMENBKRZQDR-UHFFFAOYSA-N CC=CC.[Na] Chemical compound CC=CC.[Na] JPAOMENBKRZQDR-UHFFFAOYSA-N 0.000 claims abstract description 6
- FCKYPQBAHLOOJQ-UHFFFAOYSA-N Cyclohexane-1,2-diaminetetraacetic acid Chemical compound OC(=O)CN(CC(O)=O)C1CCCCC1N(CC(O)=O)CC(O)=O FCKYPQBAHLOOJQ-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000008367 deionised water Substances 0.000 claims abstract description 6
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 6
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims abstract description 6
- 239000007921 spray Substances 0.000 claims description 5
- 239000001993 wax Substances 0.000 claims description 3
- -1 Glycol ester Chemical class 0.000 claims description 2
- AOGYCOYQMAVAFD-UHFFFAOYSA-N chlorocarbonic acid Chemical class OC(Cl)=O AOGYCOYQMAVAFD-UHFFFAOYSA-N 0.000 claims description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 2
- 239000004575 stone Substances 0.000 claims description 2
- MTHSVFCYNBDYFN-UHFFFAOYSA-N anhydrous diethylene glycol Natural products OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 abstract description 37
- PNQFGXKCAAEEAT-UHFFFAOYSA-N carbonochloridic acid;2-(2-hydroxyethoxy)ethanol Chemical compound OC(Cl)=O.OCCOCCO PNQFGXKCAAEEAT-UHFFFAOYSA-N 0.000 abstract description 5
- 150000002148 esters Chemical class 0.000 abstract description 5
- 230000018044 dehydration Effects 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000008520 organization Effects 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000003745 diagnosis Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000010827 pathological analysis Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/08—Cleaning involving contact with liquid the liquid having chemical or dissolving effect
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/10—Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/37—Polymers
- C11D3/3703—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C11D3/373—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicones
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/26—Organic compounds containing oxygen
- C11D7/261—Alcohols; Phenols
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/26—Organic compounds containing oxygen
- C11D7/266—Esters or carbonates
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/28—Organic compounds containing halogen
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/32—Organic compounds containing nitrogen
- C11D7/3245—Aminoacids
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/34—Organic compounds containing sulfur
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- General Chemical & Material Sciences (AREA)
- Detergent Compositions (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
The method that the present invention discloses paraffin in a kind of quick removal dewatering box, including following operating procedure：（1）After mixing by in-situ polymerization nano hybridization silicone oil, methylpropene sodium sulfonate, deionized water, using supersound process, dissociation agent is made；（2）1,2-cyclohexanediaminetetraacetic acid, D-ALPHA-Hydroxypropionic acid methyl esters, chloro-carbonic acid diethylene glycol (DEG) ester are added into ethyl alcohol, after being mixed evenly, then dissociation agent is added thereto, continues after being uniformly mixed, paraffin removal liquid is made；（3）Dewatering box is put into warm water, after immersion treatment, dewatering box, the moisture on the dewatering box surface that quickly exhausted with filter paper are taken out, then paraffin removal liquid is sprayed to dewatering box surface, after 5-7min, dewatering box is placed again into warm water, after immersion treatment, take out dewatering box, after being rinsed with water again, naturally dry, paraffin removal is completed in dewatering box.Method provided by the invention, can effectively remove the paraffin adhered on dewatering box, and noresidue does not interfere with reusing for dewatering box.
Description
Technical field
The invention belongs to medical detecting Instrument cleaning technique fields, and in particular to paraffin in a kind of quick removing dewatering box
Method.
Background technology
Paraffin tissue sections technology is important technology indispensable in life science, teaching, diagnosis, in paraffin group
During knitting microsection manufacture, especially pathological diagnosis and teaching, scientific experiment paraffin tissue sections manufacturing process in, dehydration
Box is one of the important equipment that can be recycled, and various tissue specimens need to be contained in respectively after number, materials each de-
In water box, main purpose is to distinguish the similar tissue in Different Individual source, while ensureing the various tissues chosen from losing.
Fixation, dehydration, transparent, waxdip of each batch tissue etc. carry out in dewatering box, after organization embedding, with organize into
The solid paraffin for entering to stick on the dewatering box of wax cylinder volume, due to being recycled in next batch histotomy manufacturing process
Dewatering box on the solid paraffin that sticks in tissue dewatering, clearing process, to be used for dimethylbenzene of transparency of organization etc. organic
Solvent dissolves, and the dimethylbenzene for having dissolved paraffin can be severely impacted on the transparent effect of purity and tissue, and then influences
To the making result of histotomy.Therefore, after organization embedding, it is necessary to at the solid paraffin that sticks on dewatering box
Reason, is removed.If the paraffin being set on dewatering box is not processed or is handled it is bad, can under the influence of batch tissue cut
To the normal use of dewatering box when piece makes.Some paraffin tissue sections production units use disposable dewatering box, although exempting
The worry of the solidification paraffin sticked on dewatering box is removed, but causes a large amount of paraffin waste, and paraffin can be caused to ring
The pollution in border.
Invention content
In order to solve the above technical problem, the present invention provides a kind of methods of paraffin in quick removing dewatering box.
The present invention is achieved by the following technical solutions.
A kind of method of paraffin in quick removing dewatering box, including following operating procedure：
（1）By weight, it is according to mass ratio by in-situ polymerization nano hybridization silicone oil, methylpropene sodium sulfonate, deionized water
10-15:1:After mixing, using 28-32min is ultrasonically treated, dissociation agent is made in 20 ratio；
（2）By weight, by 14-19 parts of 1,2-cyclohexanediaminetetraacetic acid, 3-6 parts of D-ALPHA-Hydroxypropionic acid methyl esters, 16-20 parts of chloro-carbonic acids two
Glycol ester is added into 75-85 parts of ethyl alcohol, after being mixed evenly, then 8-10 parts of steps is added thereto（1）Solution obtained
From agent, continue after being uniformly mixed, paraffin removal liquid is made；
（3）Dewatering box is put into 40-50 DEG C of warm water, after immersion treatment 3-5min, dewatering box is taken out, is quickly exhausted with filter paper
Then the moisture on dewatering box surface sprays paraffin removal liquid to dewatering box surface, after 5-7min, dewatering box is placed again into 40-
In 50 DEG C of warm water, after immersion treatment 10-12min, dewatering box is taken out, after being rinsed with water again, naturally dry, stone in dewatering box
Wax, which is removed, to be completed.
Specifically, above-mentioned steps（1）In, the purity of in-situ polymerization nano hybridization silicone oil is 99.9%.
Specifically, above-mentioned steps（1）In, the frequency size of supersound process is 28-30kHz.
Specifically, above-mentioned steps（2）In, the mass fraction of ethyl alcohol is 90-95%.
Specifically, above-mentioned steps（3）, the fountain height of paraffin removal liquid is 350-400ml/m2。
From the above technical scheme, it can be seen that the beneficial effects of the invention are as follows：
The method of paraffin, easy to operate in a kind of quick removing dewatering box provided by the invention, environmentally protective, can effectively remove
The paraffin adhered on dewatering box, noresidue do not interfere with reusing for dewatering box, in the application, paraffin removal liquid in sprinkling
Afterwards, it can be completed the cleaning to dewatering box using 40-50 DEG C of warm water, energy conservation and environmental protection, meanwhile, the ingredient in paraffin removal liquid can
It is scatter with the paraffin that will be disengaged from out so that paraffin will not condense into solid in sewer, avoid blocking sewer.Its
In, step（1）In dissociation agent obtained, may make the active force between paraffin molecule drastically to decline, can effectively avoid paraffin
There is a phenomenon where block in sewer；1,2- 1,2-diaminocyclohexane tetraacetic acids, D-ALPHA-Hydroxypropionic acid methyl esters, chloro-carbonic acid diethylene glycol (DEG) ester synergistic effect
Afterwards, permeability of the dissociation agent inside solid paraffin can be effectively promoted, and then greatly improves the elimination effect of paraffin, and
And to the paraffin at the dead angle position in dewatering box, equally there is good elimination effect, noresidue not to interfere with dewatering box
It reuses.
Specific implementation mode
In order to make the purpose , technical scheme and advantage of the present invention be clearer, following embodiment carries out the present invention
It is further described.It should be appreciated that specific embodiment party example described herein is only used to explain the present invention, it is not used to limit
The fixed present invention.
Embodiment 1
A kind of method of paraffin in quick removing dewatering box, including following operating procedure：
（1）By weight, it is according to mass ratio by in-situ polymerization nano hybridization silicone oil, methylpropene sodium sulfonate, deionized water
10:1:After mixing, using 28min is ultrasonically treated, dissociation agent is made in 20 ratio；
（2）By weight, 14 parts of 1,2-cyclohexanediaminetetraacetic acid, 3 parts of D-ALPHA-Hydroxypropionic acid methyl esters, 16 parts of chloro-carbonic acid diethylene glycol (DEG) esters are added
Enter into 75 parts of ethyl alcohol, after being mixed evenly, then 8 parts of steps is added thereto（1）It is mixed to continue stirring for dissociation agent obtained
After closing uniformly, paraffin removal liquid is made；
（3）Dewatering box is put into 40 DEG C of warm water, after immersion treatment 3min, takes out dewatering box, quickly exhausted dehydration with filter paper
Then the moisture on box surface sprays paraffin removal liquid to dewatering box surface, after 5min, dewatering box is placed again into 40 DEG C of warm water
In, after immersion treatment 10min, dewatering box is taken out, after being rinsed with water again, naturally dry, paraffin removal is completed in dewatering box.
Specifically, above-mentioned steps（1）In, the purity of in-situ polymerization nano hybridization silicone oil is 99.9%.
Specifically, above-mentioned steps（1）In, the frequency size of supersound process is 28kHz.
Specifically, above-mentioned steps（2）In, the mass fraction of ethyl alcohol is 90%.
Specifically, above-mentioned steps（3）, the fountain height of paraffin removal liquid is 350ml/m2。
Embodiment 2
A kind of method of paraffin in quick removing dewatering box, including following operating procedure：
（1）By weight, it is according to mass ratio by in-situ polymerization nano hybridization silicone oil, methylpropene sodium sulfonate, deionized water
13:1:After mixing, using 30min is ultrasonically treated, dissociation agent is made in 20 ratio；
（2）By weight, 17 parts of 1,2-cyclohexanediaminetetraacetic acid, 5 parts of D-ALPHA-Hydroxypropionic acid methyl esters, 18 parts of chloro-carbonic acid diethylene glycol (DEG) esters are added
Enter into 80 parts of ethyl alcohol, after being mixed evenly, then 9 parts of steps is added thereto（1）It is mixed to continue stirring for dissociation agent obtained
After closing uniformly, paraffin removal liquid is made；
（3）Dewatering box is put into 45 DEG C of warm water, after immersion treatment 4min, takes out dewatering box, quickly exhausted dehydration with filter paper
Then the moisture on box surface sprays paraffin removal liquid to dewatering box surface, after 6min, dewatering box is placed again into 45 DEG C of warm water
In, after immersion treatment 11min, dewatering box is taken out, after being rinsed with water again, naturally dry, paraffin removal is completed in dewatering box.
Specifically, above-mentioned steps（1）In, the purity of in-situ polymerization nano hybridization silicone oil is 99.9%.
Specifically, above-mentioned steps（1）In, the frequency size of supersound process is 29kHz.
Specifically, above-mentioned steps（2）In, the mass fraction of ethyl alcohol is 93%.
Specifically, above-mentioned steps（3）, the fountain height of paraffin removal liquid is 380ml/m2。
Embodiment 3
A kind of method of paraffin in quick removing dewatering box, including following operating procedure：
（1）By weight, it is according to mass ratio by in-situ polymerization nano hybridization silicone oil, methylpropene sodium sulfonate, deionized water
15:1:After mixing, using 32min is ultrasonically treated, dissociation agent is made in 20 ratio；
（2）By weight, 19 parts of 1,2-cyclohexanediaminetetraacetic acid, 6 parts of D-ALPHA-Hydroxypropionic acid methyl esters, 20 parts of chloro-carbonic acid diethylene glycol (DEG) esters are added
Enter into 85 parts of ethyl alcohol, after being mixed evenly, then 10 parts of steps is added thereto（1）Dissociation agent obtained, continues to stir
After mixing, paraffin removal liquid is made；
（3）Dewatering box is put into 50 DEG C of warm water, after immersion treatment 5min, takes out dewatering box, quickly exhausted dehydration with filter paper
Then the moisture on box surface sprays paraffin removal liquid to dewatering box surface, after 7min, dewatering box is placed again into 50 DEG C of warm water
In, after immersion treatment 12min, dewatering box is taken out, after being rinsed with water again, naturally dry, paraffin removal is completed in dewatering box.
Specifically, above-mentioned steps（1）In, the purity of in-situ polymerization nano hybridization silicone oil is 99.9%.
Specifically, above-mentioned steps（1）In, the frequency size of supersound process is 30kHz.
Specifically, above-mentioned steps（2）In, the mass fraction of ethyl alcohol is 95%.
Specifically, above-mentioned steps（3）, the fountain height of paraffin removal liquid is 400ml/m2。
Comparative example 1
Step（2）In, do not add step（1）Dissociation agent obtained, remaining operating procedure are identical with embodiment 1.
Same a batch, the identical dewatering box of paraffin pollution level are cleaned with the method for each embodiment and comparative example respectively
Experiment, test result are as shown in table 1：
1 dewatering box paraffin removal effect of table
It should be understood that the application of the present invention is not limited to the above, for those of ordinary skills, Ke Yigen
It is improved or converted according to above description, all these modifications and variations should all belong to the protection model of appended claims of the present invention
It encloses.
Claims (5)
1. a kind of method of paraffin in quick removing dewatering box, which is characterized in that including following operating procedure：
（1）By weight, it is according to mass ratio by in-situ polymerization nano hybridization silicone oil, methylpropene sodium sulfonate, deionized water
10-15:1:After mixing, using 28-32min is ultrasonically treated, dissociation agent is made in 20 ratio；
（2）By weight, by 14-19 parts of 1,2-cyclohexanediaminetetraacetic acid, 3-6 parts of D-ALPHA-Hydroxypropionic acid methyl esters, 16-20 parts of chloro-carbonic acids two
Glycol ester is added into 75-85 parts of ethyl alcohol, after being mixed evenly, then 8-10 parts of steps is added thereto（1）Solution obtained
From agent, continue after being uniformly mixed, paraffin removal liquid is made；
（3）Dewatering box is put into 40-50 DEG C of warm water, after immersion treatment 3-5min, dewatering box is taken out, is quickly exhausted with filter paper
Then the moisture on dewatering box surface sprays paraffin removal liquid to dewatering box surface, after 5-7min, dewatering box is placed again into 40-
In 50 DEG C of warm water, after immersion treatment 10-12min, dewatering box is taken out, after being rinsed with water again, naturally dry, stone in dewatering box
Wax, which is removed, to be completed.
2. the method for paraffin in a kind of quick removing dewatering box according to claim 1, which is characterized in that above-mentioned steps
（1）In, the purity of in-situ polymerization nano hybridization silicone oil is 99.9%.
3. the method for paraffin in a kind of quick removing dewatering box according to claim 1, which is characterized in that above-mentioned steps
（1）In, the frequency size of supersound process is 28-30kHz.
4. the method for paraffin in a kind of quick removing dewatering box according to claim 1, which is characterized in that above-mentioned steps
（2）In, the mass fraction of ethyl alcohol is 90-95%.
5. the method for paraffin in a kind of quick removing dewatering box according to claim 1, which is characterized in that above-mentioned steps
（3）, the fountain height of paraffin removal liquid is 350-400ml/m2。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810357992.1A CN108722981B (en) | 2018-04-20 | 2018-04-20 | Method for quickly removing paraffin in dehydration box |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810357992.1A CN108722981B (en) | 2018-04-20 | 2018-04-20 | Method for quickly removing paraffin in dehydration box |
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| CN108722981A true CN108722981A (en) | 2018-11-02 |
| CN108722981B CN108722981B (en) | 2021-02-05 |
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-
2018
- 2018-04-20 CN CN201810357992.1A patent/CN108722981B/en active Active
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4089703A (en) * | 1976-12-23 | 1978-05-16 | White Chemical Company, Inc. | Hot detergent process |
| JP2003313595A (en) * | 2002-04-25 | 2003-11-06 | Shinko Pantec Co Ltd | Method for decontaminating organic halogen contaminant and decontamination system for the same |
| CN103614083A (en) * | 2013-12-03 | 2014-03-05 | 沈阳化工大学 | Automobile cleaning water wax and preparation method thereof |
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Effective date of registration: 20211221 Address after: Bengbu Medical College, 2600 Donghai Avenue, Longzihu District, Bengbu City, Anhui Province 233030 Patentee after: BENGBU MEDICAL College Address before: 233000 Affiliated Hospital of Bengbu Medical College, Longzihu District, Bengbu City, Anhui Province Patentee before: Zhu Qing |