CN103215141B - Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof - Google Patents

Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof Download PDF

Info

Publication number
CN103215141B
CN103215141B CN201310135267.7A CN201310135267A CN103215141B CN 103215141 B CN103215141 B CN 103215141B CN 201310135267 A CN201310135267 A CN 201310135267A CN 103215141 B CN103215141 B CN 103215141B
Authority
CN
China
Prior art keywords
foam
radionuclide
stain remover
mass ratio
waste liquid
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.)
Expired - Fee Related
Application number
CN201310135267.7A
Other languages
Chinese (zh)
Other versions
CN103215141A (en
Inventor
林晓艳
朱高龙
罗学刚
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.)
Southwest University of Science and Technology
Original Assignee
Southwest University of Science and Technology
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 Southwest University of Science and Technology filed Critical Southwest University of Science and Technology
Priority to CN201310135267.7A priority Critical patent/CN103215141B/en
Publication of CN103215141A publication Critical patent/CN103215141A/en
Application granted granted Critical
Publication of CN103215141B publication Critical patent/CN103215141B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Detergent Compositions (AREA)

Abstract

The invention discloses a radionuclide biomass foam decontaminant capable of completely defoaming and a use method thereof. The radionuclide biomass foam decontaminant is obtained by respectively mixing sodium lauroyl sarcosine, preservatives, solubilizers, foam stabilizers and moisture at a mass ratio of 0.2%-1%:0.1%-0.5%:0.5%-7%:0.01%-1%:90.5%-99.3% and stirring at high speed. The radionuclide biomass foam decontaminant disclosed by the invention can be used for removing the contaminants positioned on a solid surface in a foam way, saving the labor power, achieving the short decontamination time of only 1-5 minutes and removing the dirt positioned at a dead angle which is difficult to contact; compared with the traditional decontamination, the radionuclide biomass foam decontaminant disclosed by the invention greatly reduces the amount of waste liquor and realizes that the amount of the waste liquor accounts for 10% of pickling; and the radionuclide biomass foam decontaminant is simple in process and low in cost and achieves the removal ratio of nuclide contaminants at 80%-90%.

Description

Radioactive nuleus cellulosic biomass foam stain remover and the using method thereof of froth breaking completely
Technical field
The invention belongs to the nucleic processing of cleaning decontamination field, be specifically related to a kind of radioactive nuleus cellulosic biomass foam stain remover and using method thereof of froth breaking completely, utilize sodium lauroyl sareosine tensio-active agent and multiple additive compound to develop the forever foam stain remover of the high clearance of froth breaking.Be specially adapted to the Sr of solid surface 2+, Th 4+deng decontamination of nucleic etc.
Background technology
Traditional solid surface decontamination method mainly contains chemical subtraction, the method that mechanical decontamination and chemical machinery decontamination combine.Though above decontamination method can effectively be removed the dirt of solid surface, can produce a large amount of waste liquids, not only increase subsequent treatment cost and also can cause secondary pollution.The method of foam decontamination can reduce waste liquid amount greatly, the short circuit of avoiding traditional decontamination method to make in a large number water cause precision instrument, the harm such as corrosion.
Existing foam stain remover detersive efficiency is on the low side, after decontamination, be difficult to can produce again a large amount of foams through certain stirring and air-blowing after froth breaking or the removal of foam, cause the liquid waste disposal of the follow-up nucleic such as evaporation, ion-exchange to be difficult to carry out, therefore a kind of froth breaking completely has the research and development of biomass foam stain remover of high soil removal efficiency significant to nucleic.So-called froth breaking completely makes after lather collapse by certain method, then by solution stir, the foaming means solution such as bubbling no longer includes foam generation.
Summary of the invention
Object of the present invention is intended to overcome deficiency of the prior art, and a kind of preparation method of radioactive nuleus cellulosic biomass foam stain remover of froth breaking is completely provided.Realize using biological material sarkosine as raw material, solve existing foam stain remover foam after decontamination and be difficult to elimination, the reluctant problem of waste liquid.
Content of the present invention is: a kind of radioactive nuleus cellulosic biomass foam stain remover of froth breaking completely: sodium lauroyl sareosine, sanitas, solubilizing agent, suds-stabilizing agent, water are mixed by 0.2%~1%, 0.1%~0.5%, 0.5%~7%, 0.01%~1% and 90.5%~99.3% mass ratio respectively, and high-speed stirring obtains foam stain remover.
Described sanitas can be one of sodium carbonate, organic amine, acid amides, Sodium Benzoate.
Described solubilizing agent can be one of ethanol, toluene, xylenesulfonate.
Described suds-stabilizing agent can be Xylo-Mucine or konjak glucomannan.
The using method of described stain remover: foam stain remover is sprayed in by radionuclide contamination surface, leave standstill 1~5min, with air-blast device, foam stain remover is removed, be collected in waste liquid barrel.The hydrochloric acid of 0.1~0.3mol/l is sprayed in the foam stain remover in waste liquid barrel, leaves standstill at normal temperatures 10-60s and treat lather collapse.Described hydrochloric acid can change makes sulfuric acid, nitric acid.
Compared with prior art, the present invention has following feature and beneficial effect:
(1) in the present invention, as whipping agent, there is precipitation in anion surfactant sodium lauroyl sareosine under certain pH conditions, and sodium lauroyl sareosine is generated water-fast Sarkosyl L by acidifying.Solving after foam decontamination a large amount of foams exists concentrated or other treatment process of lower follow-up waste liquid evaporation to be difficult to the problem of carrying out.There is larger practical value and wide application prospect;
(2) in the present invention, sodium lauroyl sareosine, complexing agent, sanitas, solubilizing agent, suds-stabilizing agent, be respectively 0.2%~1%, 0.1%~1%, 0.1%~0.5%, 0.5%~7%, 0.01%~1%, material usage is few, corrosion-free to solid surface.Hydrochloric acid is as defoamer, and raw material is easy to get, simple to operate.
(3) in the present invention, remove the pollutent of solid surface with form of foam, save manpower, the decontamination time is fast, and only 1-5min also can remove the dirt at the dead angle that is difficult for contact.Reduced greatly waste liquid amount with respect to traditional decontamination, waste liquid amount is pickling 10%.
(4) in the present invention, the implementation method of stain remover is mechanical stirring foaming, watering can spray foam, easy to operate, avoided directly contacting with human body, this formula all has removal effect to multiple pollutant, then utilizes air-blast device or mechanical vibration absorption to be had to the foam recovery of metal nucleic, spread by hand defoamer froth breaking completes decontamination froth breaking process, this invented technology is simple, with low cost, and nucleic pollutants removal rate reaches 80%-90%.
Brief description of the drawings
Fig. 1 is the infared spectrum of tensio-active agent sodium lauroyl sareosine in the present invention;
Fig. 2 is the clean effect figure of the embodiment of the present invention to Sr;
Fig. 3 is the clean effect figure of the embodiment of the present invention to U;
Fig. 4 is the surface contrast figure of (a) rear (b) before embodiment of the present invention decontamination;
Fig. 5 is the transmittance of sodium lauroyl sareosine after by acidifying;
Fig. 6 sodium lauroyl sareosine micelle-forming concentration figure.
Embodiment
Below in conjunction with specific embodiment, the present invention is described in detail.
With reference to figure 1, Fig. 5, Fig. 6, Fig. 1 is the infared spectrum of tensio-active agent sodium lauroyl sareosine in the present invention: as seen from the figure at 1706.5cm -1there is allusion quotation acid amides C=O stretching vibration; At 3321.8cm -1and 1539.5cm -1occur that acid amides N-H is flexible, formation vibration; At 1384.5cm -1there is C-N stretching vibration; At 1645.5cm -1qiang Fengwei-COONa stretching vibration.
Fig. 5 is the transmittance of sodium lauroyl sareosine after by acidifying; The sodium N-lauroyl sarcosinate solution that preparation mass ratio is 0.2%, regulates different PH to measure the variation of its transmittance.Be can be observed along with its transmittance of reduction of PH reduces gradually by Fig. 5, in the time that PH drops to 5.05, its transmitance reaches and drops to 0, and this is because sodium lauroyl sareosine and hydrochloric acid reaction generate water-fast Sarkosyl L.As can be seen from the figure do not become and clarify that bright sodium lauroyl sareosine does not have iso-electric point along with the continuation of PH reduces solution.But it can be generated water-fast Sarkosyl L by acidifying and generate white precipitate.
Along with the increase of sodium lauroyl sareosine concentration, surface tension reduces gradually as seen from Figure 6.In the time that concentration is increased to 0.003mol/l, surface tension drops to minimum.While continuing to increase concentration, surface tension increases on the contrary.So the concentration that is not tensio-active agent in the process of foaming is more high better, it is that mass ratio is in the scope of 0.03%-0.2% that its suitableeest concentration should be controlled at 0.001-0.007mol/l.
Embodiment 1:
Tensio-active agent sodium lauroyl sareosine, sanitas sodium carbonate, solubilizing agent ethanol, suds-stabilizing agent Xylo-Mucine, water mix and obtain foam detergent solution according to the mass ratio of 0.2:0.5:1:2:98.1.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
Preparation 0.5mol/l hydrochloric acid is sprayed in waste liquid barrel as defoamer, has non-foam to produce until lather collapse is observed waste liquid under high-speed stirring.The clearance of the strontium of this formula to different concns is shown in Fig. 2.
Embodiment 2:
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, water mix and obtain foam detergent solution according to the mass ratio of 0.4:0.5:1:0.1:98.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 0.5mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.The clearance of the uranium of this formula to different concns is shown in Fig. 3.
Embodiment 3:
Sodium lauroyl sareosine, sodium carbonate, ethanol, Xylo-Mucine, water mix and obtain foam detergent solution according to the mass ratio of 0.6:0.5:1:0.1:97.8.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 0.5mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.
Embodiment 4:
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, water mix and obtain foam detergent solution according to the mass ratio of 0.8:0.5:1:0.05:97.65.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 0.3mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.
Embodiment 5:
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, EDTA, water mix and obtain foam detergent solution according to the mass ratio of 1:0.5:1:0.05:0.5:96.95.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 1mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.
Embodiment 6:
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, EDTA, water mix and obtain foam detergent solution according to the mass ratio of 0.2:0.5:1:0.01:0.1:98.59.Before and after its decontamination, Fig. 4 is shown in contrast.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 1mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.
Embodiment 7:
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, EDTA, water mix and obtain foam detergent solution according to the mass ratio of 0.2:0.1:7:0.01:0.1:92.59.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 3mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.
Embodiment 8:
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, EDTA, water mix and obtain foam detergent solution according to the mass ratio of 1:0.5:2:0.05:0.5:95.95.
Obtained solution is obtained under high-speed stirring to stable foam, bubble jet is applied to contaminated surface with watering can, leave standstill 1~5min, foam is blown into and in waste liquid barrel, treats subsequent disposal with air blast blowing device.
The hydrochloric acid of preparation 2mol/l is sprayed in waste liquid barrel as defoamer, until lather collapse, observe waste liquid has non-foam to produce under high-speed stirring.
Foam height after the different embodiment froth breakings of table 1
Embodiment 1-4 does not add complexing agent EDTA, completely froth breaking.The complexing agent that embodiment 5,8 adds is too much, and foam fails thoroughly to eliminate, and as seen decontamination is had relatively high expectations, and allowing under the decontamination condition of micro-foam is can the complexing agent EDTA of additional proportion below 0.1%.
Should be understood that, for those of ordinary skills, can be improved according to the above description or convert, and all these improvement and conversion all should belong to the protection domain of claims of the present invention.

Claims (3)

1. a radioactive nuleus cellulosic biomass foam stain remover for froth breaking completely, is characterized in that,
Prepare according to following arbitrary formula:
Tensio-active agent sodium lauroyl sareosine, sanitas sodium carbonate, solubilizing agent ethanol, suds-stabilizing agent Xylo-Mucine, water mix according to the mass ratio of 0.2:0.5:1:2:98.1, and high-speed stirring obtains;
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, water mix according to the mass ratio of 0.4:0.5:1:0.1:98, and high-speed stirring obtains;
Sodium lauroyl sareosine, sodium carbonate, ethanol, Xylo-Mucine, water mix according to the mass ratio of 0.6:0.5:1:0.1:97.8, and high-speed stirring obtains;
Sodium lauroyl sareosine, sodium carbonate, ethanol, konjak glucomannan, water mix according to the mass ratio of 0.8:0.5:1:0.05:97.65, and high-speed stirring obtains.
2. the using method of foam stain remover claimed in claim 1, is characterized in that, foam stain remover is sprayed in by radionuclide contamination surface, leaves standstill 1~5min, with air-blast device, foam stain remover is removed, and is collected in waste liquid barrel; The hydrochloric acid of 0.1~0.3mol/l is sprayed in the foam stain remover in waste liquid barrel, leaves standstill at normal temperatures 10-60s and treat lather collapse.
3. the using method of foam stain remover claimed in claim 2, is characterized in that, described hydrochloric acid changes makes sulfuric acid or nitric acid.
CN201310135267.7A 2013-04-18 2013-04-18 Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof Expired - Fee Related CN103215141B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310135267.7A CN103215141B (en) 2013-04-18 2013-04-18 Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310135267.7A CN103215141B (en) 2013-04-18 2013-04-18 Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof

Publications (2)

Publication Number Publication Date
CN103215141A CN103215141A (en) 2013-07-24
CN103215141B true CN103215141B (en) 2014-10-29

Family

ID=48813310

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310135267.7A Expired - Fee Related CN103215141B (en) 2013-04-18 2013-04-18 Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof

Country Status (1)

Country Link
CN (1) CN103215141B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108085158B (en) * 2017-11-28 2020-08-07 森科(南京)医药技术有限公司 Peelable radionuclide decontaminant and preparation and use methods thereof
CN111100767A (en) * 2019-12-26 2020-05-05 郑州华核新材料科技有限公司 Nuclear power flexible hoisting belt detergent as well as preparation method and application thereof
CN111269761B (en) * 2020-02-13 2021-04-27 金丝甲(上海)安全防范技术有限公司 Decontamination liquid and application thereof in decontamination of actinide nuclide and transition metal nuclide pollution

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2827610B1 (en) * 2001-07-17 2005-09-02 Commissariat Energie Atomique DEGREASING COMPOSITION USEFUL FOR DEGREASING AND / OR DECONTAMINATING SOLID SURFACES
FR2841802B1 (en) * 2002-07-08 2005-03-04 Commissariat Energie Atomique COMPOSITION, FOAM AND METHOD FOR DECONTAMINATING SURFACES
US7166758B2 (en) * 2005-03-26 2007-01-23 Luis Nunez Foam and gel methods for the decontamination of metallic surfaces
CN102899206B (en) * 2012-11-14 2014-07-09 西南科技大学 Preparation and use method of radionuclide decontaminant

Also Published As

Publication number Publication date
CN103215141A (en) 2013-07-24

Similar Documents

Publication Publication Date Title
CN100497571C (en) Solar energy silicon crystal chip cleaning agent
CN103215141B (en) Radionuclide biomass foam decontaminant capable of completely defoaming and use method thereof
CN104403811A (en) Nano inorganic material and alkyl glycoside compounded radionuclide decontaminant as well as use method thereof
CN104190472B (en) A kind of new and effective multiphase Fenton catalyst Fe 3O4@EDTA preparation and application
CN104512974A (en) Method for deeply removing persistent organic pollutants and heavy metal in water body
CN104389011B (en) Electrochemical decontamination electrolyte
CN108392969A (en) A kind of formaldehyde removal purification spray
CN204735114U (en) Exhaust treatment device of steam power plant
WO2015158239A1 (en) Fume desulfurization and denitrification method
CN103691280B (en) A kind of method and system removing gas mercury based on ultrasonic excitation sodium peroxydisulfate
CN108911016A (en) A kind of flocculant for sewage treatment
CN205442874U (en) Economical thermal power plant contains ammonia wastewater processing system
CN107698004A (en) Preparation method with the high polymer coagulant for removing cadmium function
CN104289216B (en) For the ozone catalyst of Surfactant-Catalyzed of degrading and preparation thereof and application
CN102688677B (en) Method for enhancing total mercury recovery rate of metallurgical fume by reducing bivalent mercury
CN102569065A (en) Acid washing process of diode chip
CN104877777A (en) Water-based detergent and preparation method and application thereof
CN107879502A (en) A kind of processing method of formaldehyde waste water
CN204779152U (en) Liquid water disposal recovery system of stainless steel pickling line
CN207525093U (en) Remove the equipment of spent acid and heavy metal in waste water
CN106045065A (en) Municipal sewage environmental-protection treating agent
CN104099193A (en) Water-based glass cleaning agent and its preparation method and use in mobile phone lens cleaning
CN104529005A (en) Multistage combined flocculation device and process for selectively removing aconitine type toxic ingredients from traditional Chinese medicine processing wastewater by using same
CN205528220U (en) Salt -containing waste water treating device
CN205549979U (en) Desulfidation dedusting system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141029

Termination date: 20150418

EXPY Termination of patent right or utility model