CN103710171A - Acidic solid cleaning agent and preparation method thereof - Google Patents

Acidic solid cleaning agent and preparation method thereof Download PDF

Info

Publication number
CN103710171A
CN103710171A CN201310713203.0A CN201310713203A CN103710171A CN 103710171 A CN103710171 A CN 103710171A CN 201310713203 A CN201310713203 A CN 201310713203A CN 103710171 A CN103710171 A CN 103710171A
Authority
CN
China
Prior art keywords
cleaning agent
nitric acid
solid cleaning
acidic solid
urea
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
CN201310713203.0A
Other languages
Chinese (zh)
Inventor
牛志刚
吴文琴
杨联
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.)
Inner Mongolia Hexi Aerospace Science & Technology Development Co Ltd
Original Assignee
Inner Mongolia Hexi Aerospace Science & Technology Development 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 Inner Mongolia Hexi Aerospace Science & Technology Development Co Ltd filed Critical Inner Mongolia Hexi Aerospace Science & Technology Development Co Ltd
Priority to CN201310713203.0A priority Critical patent/CN103710171A/en
Publication of CN103710171A publication Critical patent/CN103710171A/en
Pending legal-status Critical Current

Links

Abstract

The invention relates to an acidic solid cleaning agent. The acidic solid cleaning agent is an acicular crystal product separated from a reaction of nitric acid and urea, and the composition ratio of nitric acid to urea can be properly and freely added according to nitric acid concentration and the preparation demand. The acidic solid cleaning agent is prepared by the following steps: firstly, preparing water bath, and maintaining the temperature at 25-95 DEG C; adding nitric acid into a reaction container, and stirring; adding urea, and continuously stirring after urea is dissolved; cooling the stirred mixture in a cooling device at a cooling temperature of minus 5 to 20 DEG C, and stirring to generate acicular crystals; separating the generated acicular crystals to obtain the acidic solid cleaning agent. After being dissolved in water, the acidic solid cleaning agent provided by the invention is mainly used for cleaning the inner surfaces of such apparatuses as container, pipeline and the like in a dairy product processing process, the acidic solid cleaning agent is convenient to transport and use, and meanwhile, the acidic solid cleaning agent has the advantages of effectively reducing or eliminating nitrite in the system.

Description

A kind of solid acid clean-out system and preparation method
Technical field
The present invention relates to a kind of solid acid clean-out system, particularly solid acid clean-out system and preparation method for Dairy Industry equipment.
Background technology
Traditional Dairy Industry equipment washing is used liquid ceanser, in transportation, easily reveals and drops, and uses and also easily occurs the phenomenon that part solute solidifies simultaneously under cold condition, to use, makes troubles.
Summary of the invention
This technical problem that will solve is to provide a kind of solid acid clean-out system, to solve equipment washing, use liquid ceanser, in transportation, easily reveal and drop, under cold condition, use and also easily occur the phenomenon that part solute solidifies simultaneously, to use, make troubles, the problem of the solid acid clean-out system that the Dairy Industry equipment surface of highly effective and safe clean to be used is provided.
For solving the technical problem existing, the technical solution used in the present invention is: solid acid clean-out system is the nitric acid needle crystal product separated with urea reaction.
The mother liquor of solid acid clean-out system preparation process of the present invention can be used continuously, thus, the component proportion of nitric acid and urea can need to carry out suitable free proportioning interpolation according to concentration of nitric acid and preparation, it is example that the nitric acid that mass concentration is 68% is take in the present invention, preferably the mass ratio of nitric acid and urea is 5~0.5, the quality that the nitric acid of other concentration can convert and use according to the nitric acid of above-mentioned concentration.
The preparation method of solid acid clean-out system, concrete steps are as follows:
1) be ready to water-bath, temperature remains on 25 ℃~95 ℃;
2) nitric acid is joined in reaction vessel, stir;
3) add urea, after dissolving, continue again to stir;
4) mixture being uniformly mixed is put into refrigerating unit cooling, cooling temperature is-5 ℃~20 ℃, produces while stirring needle crystal;
5) needle crystal producing is separated, obtain solid acid clean-out system.
Use solid acid clean-out system of the present invention to compare traditional liquid acidic clean-out system, in transportation, there is clear superiority, product is packaged convenience not only, in transportation, do not worry losing loose leakage problem, and freight charges significantly reduce before, with 48% traditional liquid clean-out system, calculate, freight charges are saved and are surpassed 50%.
Solid acid clean-out system of the present invention is dissolved in the cleaning that is mainly used in the internal surface of the equipment such as container used in diary product process, pipeline after water, the present invention can solve equipment washing and use liquid ceanser, in transportation, easily reveal and drop, under cold condition, use and also easily occur the phenomenon that part solute solidifies simultaneously, to use, make troubles, the problem of the solid acid clean-out system that the Dairy Industry equipment surface of highly effective and safe clean to be used is provided, meanwhile, also there is effective minimizing or the system of elimination nitrite.
Embodiment
Below in conjunction with specific embodiment, the invention will be further described.
Use nitric acid and urea to make solid acid clean-out system by certain technique, wherein, nitric acid (68% the nitric acid of take is example, and other concentration can be used according to the mass conversion of nitric acid) is 5~0.5 with the weight ratio of urea, and synthetic method comprises the steps:
1) be ready to water-bath, constant temperature to 25 ℃~95 ℃;
2) nitric acid is joined in reaction vessel, stir;
3) add urea, after dissolving, continue again to stir 1 hour;
4) mixture being uniformly mixed is put into refrigerating unit cooling, cooling temperature is-5 ℃~20 ℃, produces while stirring needle crystal;
5) above process is carried out after 6 hours~14 hours, centrifugation, and mother liquor is stayed and is continued next time to use.
Embodiment 1: constant temperature water bath to 50 ℃, take 68% nitric acid 80g, add in 250mL beaker, then add urea 50g, continue to stir 1 hour, beaker is moved in refrigerating unit, 10 ℃ of cooling temperatures, maintain and stir 10 hours, produce needle crystal product, after centrifugation, mother liquor leaves time use.
Embodiment 2: working method is with embodiment 1, and bath temperature changes 75 ℃ into, obtains needle crystal product.
Embodiment 3: working method is with embodiment 2, and cooling temperature changes-5 ℃ of g into, obtains needle crystal product.
Embodiment 4: working method is with embodiment 2, and the cooling and stirring time changes 14 hours into, obtains needle crystal product.
Embodiment 5: working method is with embodiment 1, and bath temperature changes 90 ℃ into and changes, and obtains needle crystal product.

Claims (3)

1. a solid acid clean-out system is nitric acid and needle crystal product separated after urea reaction.
2. solid acid clean-out system according to claim 1, is characterized in that: the mass ratio of nitric acid and urea is 5~0.5, and wherein, the mass concentration of nitric acid is 68%.
3. the preparation method of solid acid clean-out system according to claim 1 and 2, concrete steps are as follows:
1) be ready to water-bath, temperature remains on 25 ℃~95 ℃;
2) nitric acid is joined in reaction vessel, stir;
3) add urea, after dissolving, continue again to stir;
4) mixture being uniformly mixed is put into refrigerating unit cooling, cooling temperature is-5 ℃~20 ℃, produces while stirring needle crystal;
5) needle crystal producing is separated, mother liquor is stayed and is continued next time to use.
CN201310713203.0A 2013-12-12 2013-12-12 Acidic solid cleaning agent and preparation method thereof Pending CN103710171A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310713203.0A CN103710171A (en) 2013-12-12 2013-12-12 Acidic solid cleaning agent and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310713203.0A CN103710171A (en) 2013-12-12 2013-12-12 Acidic solid cleaning agent and preparation method thereof

Publications (1)

Publication Number Publication Date
CN103710171A true CN103710171A (en) 2014-04-09

Family

ID=50403534

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310713203.0A Pending CN103710171A (en) 2013-12-12 2013-12-12 Acidic solid cleaning agent and preparation method thereof

Country Status (1)

Country Link
CN (1) CN103710171A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11214763B2 (en) 2018-01-26 2022-01-04 Ecolab Usa Inc. Solidifying liquid amine oxide, betaine, and/or sultaine surfactants with a carrier
US11377628B2 (en) 2018-01-26 2022-07-05 Ecolab Usa Inc. Solidifying liquid anionic surfactants
US11655436B2 (en) 2018-01-26 2023-05-23 Ecolab Usa Inc. Solidifying liquid amine oxide, betaine, and/or sultaine surfactants with a binder and optional carrier

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2132511A (en) * 1934-06-23 1938-10-11 Henkel & Cie Gmbh Cleaning composition and method
CN1583716A (en) * 2004-06-14 2005-02-23 陕西福奥特实业有限公司 Preparing method for inactive nitric acid powder
CN102491858A (en) * 2011-12-20 2012-06-13 上海化工研究院 Method for manufacturing urea-based nitrate slow-releasing compound fertilizer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2132511A (en) * 1934-06-23 1938-10-11 Henkel & Cie Gmbh Cleaning composition and method
CN1583716A (en) * 2004-06-14 2005-02-23 陕西福奥特实业有限公司 Preparing method for inactive nitric acid powder
CN102491858A (en) * 2011-12-20 2012-06-13 上海化工研究院 Method for manufacturing urea-based nitrate slow-releasing compound fertilizer

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
荣国斌等: "《大学有机化学基础》", 31 August 2000, 华东理工大学出版社,化学工业出版社 *
陈颖超等: "硝酸脲的制备", 《天津化工》 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11214763B2 (en) 2018-01-26 2022-01-04 Ecolab Usa Inc. Solidifying liquid amine oxide, betaine, and/or sultaine surfactants with a carrier
US11377628B2 (en) 2018-01-26 2022-07-05 Ecolab Usa Inc. Solidifying liquid anionic surfactants
US11655436B2 (en) 2018-01-26 2023-05-23 Ecolab Usa Inc. Solidifying liquid amine oxide, betaine, and/or sultaine surfactants with a binder and optional carrier
US11834628B2 (en) 2018-01-26 2023-12-05 Ecolab Usa Inc. Solidifying liquid anionic surfactants

Similar Documents

Publication Publication Date Title
CN103710171A (en) Acidic solid cleaning agent and preparation method thereof
CN107418521B (en) Ternary phase change cold storage material and preparation method thereof
MX2017010418A (en) Method for continuous preparation of high bulk density methionine crystal.
CN104016384A (en) Method of preparing high-purity cesium carbonate and high-purity rubidium carbonate
US10173972B2 (en) Method for producing high-purity aqueous urea solution in urea production process
CN101935840B (en) Compound octadecylamine corrosion inhibitor and preparation method thereof
CN104891466B (en) Production method of instant food-grade sodium pyrophosphate
CN106629784B (en) A kind of technique of adding halogen method production rice-shaped crystallization potassium nitrate
CN105036098A (en) Method for removing sodium carbonate in solution
CN102786864A (en) Anticorrosive paint for rusty coating and preparation method of anticorrosive paint
CN105886143A (en) Low-price environment-friendly weakly-acid cleaning agent
CN205387483U (en) In succession freezing crystal separation system for waste water
CN103596916A (en) Method for reducing fouling during purification of (meth)acrylate esters
CN107651699A (en) A kind of production method of technical grade potassium nitrate
CN104829585B (en) A kind of piperonal crystallization preparation technology
CN104086234B (en) The industrial process of urea ammonium nitrate Water soluble fertilizer
CN109777669A (en) A kind of degreaser
US10519103B2 (en) Urea production method
CN102191506A (en) Production method of nano deruster
CN101880064A (en) Method for producing sodium permanganate
CN104987492B (en) A kind of thick anti-condensation additives of TDI and its application method
Zhou et al. Efficient absorption of low pressure NH3 by non-ionic phenol-based deep eutectic solvents with multiple acidic sites
SG11201808954RA (en) Method for purifying methacrylic acid and method for producing methacrylic acid
CN102994149B (en) Corrosion-retarding agent and preparation method thereof, and method for reducing acid-containing hydrocarbon oil corrosivity
CN103396530A (en) Synthesizing method of p-cresol-dicyclopentadiene isobutyl resin antioxidant

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140409