CN104232343A - Sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries and application thereof - Google Patents
Sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries and application thereof Download PDFInfo
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Abstract
The invention provides a sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries. The sugar material cleaning agent is a water-based cleaning agent which comprises the following components in percentage by weight: 0.1-5.0% of alkaline inorganic matters, 0.5-5.0% of a surfactant and 90.0-99.4% of water. The invention further provides use of the sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries. The sugar material cleaning agent is free from corrosion to stainless steel production equipment, high in soil removal efficiency, good in cleaning effect and free from residues, is used for effectively eliminating residual sugar materials in production equipment of tobacco and food industries, and can be used for avoiding peculiar smell and tainting by other odor. The used components are low in cost and safe and non-toxic.
Description
Technical field
The present invention relates to the cleaning technique field of production unit, being specifically related to sugar material clean-out system and the application thereof of residual sugar material in a kind of production unit for cleaning tobacco and food service industry.
Background technology
Sugar is aldehydes (Aldehyde) or ketone (Ketone) compound of a kind of poly-hydroxy (2 or more), as the nutritive ingredient of needed by human, be converted into carbohydrate, for body energy after absorption of human body at once.At present, human body mainly through taking in sugar from tobacco, food etc., and therefore, sugar, as one of raw material most important in tobacco and food, is widely used in the production of tobacco and food service industry.
But in the actual production process of tobacco and food service industry, sugar material, as important interpolation raw material, is easy to remain in production unit as in storage tank and tubing system.Before remaining liquid residual in storage tank and tubing system after a collection of products production, pleasant impression, particle residual assorted, applying ratio and precision that tank (pipe) wall incrustation can affect next batch product feed liquid, cause peculiar smell and taint of odour between product, affect the quality of product.Therefore, need a kind of clean-out system regularly to for the production of storage tank and tubing system effectively clean, thoroughly eliminate sugar material residual in the production unit of tobacco and food service industry, avoid hidden danger of quality and the accident of peculiar smell and taint of odour between product.
Meanwhile, this kind of clean-out system should be nontoxic, and do not produce burn into destruction to the storage tank produced and tubing system.And at present, in the production unit of this low toxicity, efficiently tobacco and food service industry, sugar material clean-out system has no report, highly the practitioner of the industry carries out deep research and exploration.
Summary of the invention
The shortcoming of prior art in view of the above, the object of the present invention is to provide sugar material clean-out system and the application thereof of residual sugar material in a kind of production unit for cleaning tobacco and food service industry, effectively eliminating sugar material residual in the production unit of tobacco and food service industry for solving in prior art to lack, avoiding the hidden danger of quality of peculiar smell and taint of odour and the problem of accident between product.
For achieving the above object, the invention provides the sugar material clean-out system of residual sugar material in a kind of production unit for cleaning tobacco and food service industry, described sugar material clean-out system is aqueous cleaning agent, by weight percentage, comprises following component:
Alkali inorganic substance 0.1-5.0%;
Tensio-active agent 0.5-5.0%;
Water 90.0-99.4%.
Preferably, described alkali inorganic substance is selected from the one in sodium hydroxide, sodium acetate, sodium carbonate, clorox.
Described alkali inorganic substance refers to and can be dissolved in water completely, and the mineral compound that the pH value forming the aqueous solution is greater than 7.0.
Further, No. CAS of described sodium hydroxide is 1310-73-2; No. CAS of described sodium acetate is 127-09-3; No. CAS of described sodium carbonate is 497-19-8; No. CAS of described clorox is 7681-52-9.
Preferably, described tensio-active agent is selected from the one in sodium lauryl sulphate and lauryl glucosyl.
Further, No. CAS of described sodium lauryl sulphate is 151-21-3; No. CAS of described lauryl glucosyl is 110615-47-9.
Preferably, described water is distilled water.
Preferably, described sugar material clean-out system, by weight percentage, comprises following component:
Alkali inorganic substance 0.5-2.0%;
Tensio-active agent 3.0-5.0%;
Water 93.0-96.5%.
The invention discloses the preparation method of sugar material clean-out system described above, comprise the following steps: by alkali inorganic substance and surfactant dissolves in water, stir.
The invention also discloses the purposes of sugar material clean-out system described above residual sugar material in the production unit cleaning tobacco and food service industry.
Described production unit refers to feed liquid hold-up vessel, feed liquid preparing tank and feed liquid transport pipe.
The invention discloses the purging method of the sugar material clean-out system of residual sugar material in the above-mentioned production unit for cleaning tobacco and food service industry, comprising the following steps:
1), after the sugar material clean-out system prepared being heated, inject production unit, production unit is soaked;
2), after soaking, clean-out system is entered Sewage treatment systems;
3) after being soaked by production unit clear water again, clear water is entered Sewage treatment systems, finally equipment is dried and can put into production again.
Preferably, as step 1) as described in sugar material clean-out system Heating temperature be 20-70 DEG C.More excellent, the Heating temperature of described sugar material clean-out system is 50-60 DEG C.
Preferably, as step 1) as described in sugar material clean-out system be 0.5-12 hour to the time that production unit soaks.More excellent, described sugar material clean-out system is 1-2 hour to the time that production unit soaks.
Described Sewage treatment systems is that factory collects and the system processed the waste water produced in production process, and it is connected with production unit.
Preferably, as step 3) as described in clear water be distilled water.
Preferably, as step 3) as described in clear water be 0.5-5 hour to the time that production unit soaks.More excellent, described clear water is 1-2 hour to the time that production unit soaks.
Preferably, as step 3) as described in dry for natural air drying.
As mentioned above, the sugar material clean-out system of residual sugar material and application thereof in a kind of production unit for cleaning tobacco and food service industry of the present invention, have following beneficial effect:
1. the sugar material clean-out system of residual sugar material in a kind of production unit for cleaning tobacco and food service industry of the present invention, uses weakly alkaline aqueous cleaning agent, for stainless steel production unit non-corrosiveness.
2. the sugar material clean-out system of residual sugar material in a kind of production unit for cleaning tobacco and food service industry of the present invention, soil removal efficiency is high, reach as high as 99.9%, cleaning performance is good, noresidue, the sugar material that effective elimination is residual in the production unit of tobacco and food service industry, avoids peculiar smell and taint of odour between product.
3. the sugar material clean-out system of residual sugar material in a kind of production unit for cleaning tobacco and food service industry of the present invention, the component of use is conventional reagent, and cost is low, safety non-toxic.
Accompanying drawing explanation
Fig. 1 is shown as the sugar material clean-out system operation schematic flow sheet of residual sugar material in a kind of production unit for cleaning tobacco and food service industry of the present invention
Embodiment
Set forth the present invention further below in conjunction with specific embodiment, should be understood that these embodiments are only not used in for illustration of the present invention and limit the scope of the invention.
Below by way of specific specific examples, embodiments of the present invention are described, those skilled in the art the content disclosed by this specification sheets can understand other advantages of the present invention and effect easily.The present invention can also be implemented or be applied by embodiments different in addition, and the every details in this specification sheets also can based on different viewpoints and application, carries out various modification or change not deviating under spirit of the present invention.
The equipment that embodiment uses is as follows:
RBHX-II type crust pendulum washes machine (China Daily Chemical Industry Research Institute); 304 stainless steel steel discs (China Daily Chemical Industry Research Institute); Chemical oxygen demand (COD) (COD) determinator (Hach company of the U.S.)
Embodiment 1
With reference to the measuring method of washing power in People's Republic of China (PRC) light industry industry standard QB/T 2117-1995 " general water-base metal detergent ", the sugar material clean effect of clean-out system in the present invention is evaluated, to assess the potential use of clean-out system in the production unit of tobacco and food service industry in the cleaning of sugar material.At ambient temperature, 1.5g sodium hydroxide and 3.0g sodium lauryl sulphate are dissolved in 295.5g water, prepare the sodium hydroxide clean-out system that weight percent is 0.5%, get a certain amount of 0.5% sodium hydroxide clean-out system respectively, make its temperature remain on 20,30,40,50,60,70 DEG C.Select polylith 304 stainless steel steel disc as test piece, weigh and be recorded as m
0; In test piece, apply the sugared doses of about 0.4g respectively, after dry, cooling is weighed, and is recorded as m
1.Test piece is made to be immersed in 0.5% sodium hydroxide clean-out system of differing temps respectively, soak time is 30s, then adopt RBHX-II type crust to put to wash the machine time of carrying out be that the pendulum of 30s is washed, and taking out the laggard line time of test piece is after the water pendulum of 30s is washed, after carrying out drying again, cooling is weighed, and is recorded as m
2.Calculate sugar material soil removal efficiency, concrete data are in table 1.
The calculation formula of sugar material soil removal efficiency is: X
1for=(m
1-m
2)/(m
1-m
0) × 100; Wherein, X
1for washing power, %; m
0for test piece quality, g; m
1for applying the quality before sugar material test piece cleaning, g; m
2for applying the quality after sugar material test piece cleaning, g.
Table 1 differing temps is on the impact of the sugar material clean effect of clean-out system
Table 1 result illustrates that the clean effect of temperature on clean-out system of clean-out system has remarkably influenced, the rising of clean-out system temperature is conducive to the clean effect improving clean-out system, but tend to balance gradually, when namely clean-out system temperature is respectively 60 and 70 DEG C, soil removal efficiency remains unchanged substantially.Due in process of production, heated wash agent needs certain energy consumption, therefore considers from soil removal efficiency and energy consumption two combined factors, and the Heating temperature of sugar material clean-out system is preferably 50-60 DEG C.
Embodiment 2
As the measuring method of washing power in embodiment 1, the sugar material clean effect of clean-out system in the present invention is evaluated.Adopt weight percent to be 0.5% sodium hydroxide clean-out system (component formula is as embodiment 1), make its temperature remain on 20 DEG C.Test piece applies the sugared doses of about 0.4g, adopt different mode of washing (comprise soak time, pendulum wash the time, water pendulum wash the time), calculate sugar material soil removal efficiency, concrete data are in table 2.
The different mode of washing of table 2 is on the impact of the sugar material clean effect of clean-out system
Table 2 result illustrates that the clean effect of mode of washing on clean-out system of clean-out system has remarkably influenced, immersion significantly can reduce the clinging power of sugar material in test piece, clean-out system also a certain amount of sugar material of solubilized in immersion process, makes clean-out system have the soil removal efficiency of 17.0% simultaneously; If change immersion into pendulum to wash, namely on the basis of action of soaking, add External Force Acting, sugar material is easilier removed from test piece, thus significantly improves the soil removal efficiency of clean-out system to sugar material, reach 35.1%; If first reducing the clinging power of sugar material in test piece by soaking, then carrying out pendulum and washing, then the soil removal efficiency of clean-out system can be increased to 40.3% further; If to soak and after pendulum washes at clean-out system, then carry out water pendulum and wash, in this process, remove the sugar material that test piece is adhered to by External Force Acting further, soil removal efficiency rises to 67.9%.As shown in Table 2, when wash conditions is chosen as respectively, soak time is 30s, the pendulum time of washing is 30s, the water pendulum time of washing, when being 30s, it is best that the clean effect that in production unit, sugar material is residual removed by 0.5% sodium hydroxide clean-out system.
Embodiment 3
As the measuring method of washing power in embodiment 1, the sugar material clean effect of sodium hydroxide clean-out system in the present invention is evaluated.Adopt weight percent to be 0.5% sodium hydroxide clean-out system (component formula is as embodiment 1), make its temperature remain on 20 DEG C.Test piece applies the sugared doses of about 0.4g, adopts different pendulum to wash the time, calculate sugar material soil removal efficiency, concrete data are in table 3.
Table 3 pendulum washes the impact of time on the sugar material clean effect of clean-out system
Table 3 result illustrates that the pendulum time of washing has remarkably influenced to removing of sugar material in test piece, and extend pendulum and wash the time, residual sugared doses constantly reduces.When to wash selection of time be 150s to pendulum, it is best that the clean effect that in production unit, sugar material is residual removed by 0.5% sodium hydroxide clean-out system.
Embodiment 4
As the measuring method of washing power in embodiment 1, the sugar material clean effect of sodium acetate clean-out system in the present invention is evaluated.At ambient temperature, 1.5g sodium acetate and 3.0g sodium lauryl sulphate are dissolved in 295.5g water, prepare the sodium acetate clean-out system that weight percent is 0.5%, make its temperature remain on 20 DEG C.Test piece applies the sugared doses of about 0.4g, employing soak time is 30s, the pendulum time of washing is 30s, the water pendulum time of washing is the mode of washing of 30s, and adopts method in embodiment 1 to calculate sugar material soil removal efficiency, concrete data are in table 4.
Embodiment 5
As the measuring method of washing power in embodiment 1, the sugar material clean effect of sodium carbonate clean-out system in the present invention is evaluated.At ambient temperature, 1.5g sodium carbonate and 3.0g sodium lauryl sulphate are dissolved in 295.5g water, prepare the sodium carbonate clean-out system that weight percent is 0.5%, make its temperature remain on 20 DEG C.Test piece applies the sugared doses of about 0.4g, employing soak time is 30s, the pendulum time of washing is 30s, the water pendulum time of washing is the mode of washing of 30s, and adopts method in embodiment 1 to calculate sugar material soil removal efficiency, concrete data are in table 4.
Embodiment 6
As the measuring method of washing power in embodiment 1, the sugar material clean effect of clorox clean-out system in the present invention is evaluated.At ambient temperature, 1.5g clorox and 3.0g lauryl glucosyl are dissolved in 295.5g water, prepare the clorox clean-out system that weight percent is 0.5%, make its temperature remain on 20 DEG C.Test piece applies the sugared doses of about 0.4g, employing soak time is 30s, the pendulum time of washing is 30s, the water pendulum time of washing is the mode of washing of 30s, and adopts method in embodiment 1 to calculate sugar material soil removal efficiency, concrete data are in table 4.
The clean effect of table 4 different sorts clean-out system
As shown in Table 4, different sorts clean-out system is under identical washing Force meansurement condition, and the clean effect removing sugar material residual is similar, can mutually replace in actual use.
Embodiment 7
By weight percent be 0.5% sodium hydroxide clean-out system to be used in the production unit of tobacco and food service industry the cleaning of sugar material, wherein, the weight percent of sodium lauryl sulphate is 0.5%.The temperature of clean-out system is respectively 20,30,40,50,70 DEG C, and the time of clean-out system soaking device is 2 hours.Adopt COD determinator to detect the organic content in clean-out system, initial COD value is C
0, soaking COD value after 2 hours is C
1, will extend soak time until COD value is constant, now COD value is C
2.Calculate sugar material soil removal efficiency, concrete data are in table 5.
The calculation formula of sugar material soil removal efficiency is: X
1for=(C
0-C
1)/(C
0-C
2) × 100; Wherein, X
1for washing power, %; C
0for COD value initial in clean-out system, mg/L; C
1for soaking the COD value of clean-out system after 2 hours, mg/L; C
2for soaking certain hour until COD value when the COD value of clean-out system is constant, mg/L.
The different soaking temperature of table 5 is on the impact of sugar material clean effect in production unit
| Alkali inorganic substance | Concentration (%) | Temperature (DEG C) | Soak time (h) | Soil removal efficiency (%) |
| Sodium hydroxide | 0.5 | 20 | 2 | 90.5 |
| Sodium hydroxide | 0.5 | 30 | 2 | 93.1 |
| Sodium hydroxide | 0.5 | 40 | 2 | 97.5 |
| Sodium hydroxide | 0.5 | 50 | 2 | 99.9 |
| Sodium hydroxide | 0.5 | 70 | 2 | 99.9 |
As shown in Table 5, when soaking temperature is more than 50 DEG C, sodium hydroxide clean-out system can reach best effect to sugar material clean effect in production unit, and soil removal efficiency reaches as high as 99.9%.After test, clean-out system is entered Sewage treatment systems, use clear water to soak 2 hours, clear water is entered Sewage treatment systems, dries equipment stand-by.
Embodiment 8
Be the sodium hydroxide clean-out system of 0.5% by weight percent, for the cleaning of sugar material in the production unit of tobacco and food service industry, wherein, the weight percent of sodium lauryl sulphate is 5.0%.The temperature of clean-out system is respectively 50 DEG C, and the time of clean-out system soaking device is respectively 0.5,1,2,4,12 hour.Adopt COD determinator to detect the organic content in clean-out system, initial COD value is C
0, after immersion for some time, COD value is C
1, extend soak time until COD value is constant, now COD value is C
2.Calculate sugar material soil removal efficiency, concrete data are in table 6.
The calculation formula of sugar material soil removal efficiency is: X
1for=(C
0-C
1)/(C
0-C
2) × 100; Wherein, X
1for washing power, %; C
0for COD value initial in clean-out system, mg/L; C
1for soaking the COD value of clean-out system after 0.5,2,4,12 hour respectively, mg/L; C2 soaks certain hour until COD value when the COD value of clean-out system is constant, mg/L.
The different soak time of table 6 is on the impact of sugar material clean effect in production unit
| Alkali inorganic substance | Concentration (%) | Temperature (DEG C) | Soak time (h) | Soil removal efficiency (%) |
| Sodium hydroxide | 0.5 | 50 | 0.5 | 94.2 |
| Sodium hydroxide | 0.5 | 50 | 1 | 98.3 |
| Sodium hydroxide | 0.5 | 50 | 2 | 99.9 |
| Sodium hydroxide | 0.5 | 50 | 4 | 99.9 |
| Sodium hydroxide | 0.5 | 50 | 12 | 99.9 |
As shown in Table 6, when soak time is 1-2 hour, sodium hydroxide clean-out system can reach best effect to sugar material clean effect in production unit, and soil removal efficiency can reach 98.3-99.9%.After test, clean-out system is entered Sewage treatment systems, use clear water to soak 1 hour, clear water is entered Sewage treatment systems, dries equipment stand-by.
Embodiment 9
Weight percent is respectively the sodium hydroxide clean-out system of 0.1,0.3,0.5,1.0,3.0,5.0%, add the sodium lauryl sulphate that weight percent is 3.0% respectively, for the cleaning of sugar material in the production unit of tobacco and food service industry, the temperature of clean-out system is respectively 50 DEG C, and the time of clean-out system soaking device is 2 hours.Adopt COD determinator to detect the organic content in clean-out system, initial COD value is C
0, soaking COD value after 2 hours is C
1, extend soak time until COD value is constant, now COD value is C
2.Calculate sugar material soil removal efficiency, concrete data are in table 7.
The calculation formula of sugar material soil removal efficiency is: X
1for=(C
0-C
1)/(C
0-C
2) × 100; Wherein, X
1for washing power, %; C
0for COD value initial in clean-out system, mg/L; C
1for soaking the COD value of clean-out system after 2 hours, mg/L; C
2for soaking certain hour until COD value when the COD value of clean-out system is constant, mg/L.
The clean-out system of table 7 Different Weight per-cent is on the impact of sugar material clean effect in production unit
| Alkali inorganic substance | Concentration (%) | Temperature (DEG C) | Soak time (h) | Soil removal efficiency (%) |
| Sodium hydroxide | 0.1 | 50 | 2 | 85.2 |
| Sodium hydroxide | 0.3 | 50 | 2 | 91.4 |
| Sodium hydroxide | 0.5 | 50 | 2 | 99.9 |
| Sodium hydroxide | 1.0 | 50 | 2 | 99.9 |
| Sodium hydroxide | 3.0 | 50 | 2 | 99.9 |
| Sodium hydroxide | 5.0 | 50 | 2 | 99.9 |
As shown in Table 7, when the weight percent of sodium hydroxide clean-out system is more than 0.5%, sodium hydroxide clean-out system can reach best effect to sugar material clean effect in production unit, and soil removal efficiency can reach 99.9%.After test, clean-out system is entered Sewage treatment systems, use clear water to soak 5 hours, clear water is entered Sewage treatment systems, dries equipment stand-by.
Embodiment 10
Selection weight percent is sodium hydroxide, sodium acetate, sodium carbonate, the clorox clean-out system of 0.5% respectively, add the lauryl glucosyl that weight percent is 3.0% respectively, for the cleaning of sugar material in the production unit of tobacco and food service industry, the temperature of clean-out system is respectively 50 DEG C, and the time of clean-out system soaking device is 2 hours.Adopt COD determinator to detect the organic content in clean-out system, initial COD value is C
0, soaking COD value after 2 hours is C
1, extend soak time until COD value is constant, now COD value is C
2.Calculate sugar material soil removal efficiency, concrete data are in table 8.
The calculation formula of sugar material soil removal efficiency is: X
1for=(C
0-C
1)/(C
0-C
2) × 100; Wherein, X
1for washing power, %; C
0for COD value initial in clean-out system, mg/L; C
1for soaking the COD value of clean-out system after 2 hours, mg/L; C
2for soaking certain hour until COD value when the COD value of clean-out system is constant, mg/L.
Table 8 different sorts clean-out system is on the impact of sugar material clean effect in production unit
| Alkali inorganic substance | Concentration (%) | Temperature (DEG C) | Soak time (h) | Soil removal efficiency (%) |
| Sodium hydroxide | 0.5 | 50 | 2 | 99.9 |
| Sodium acetate | 0.5 | 50 | 2 | 99.9 |
| Sodium carbonate | 0.5 | 50 | 2 | 99.9 |
| Clorox | 0.5 | 50 | 2 | 99.9 |
As shown in Table 8, under the same conditions, the clean effect removing tobacco residual with sugar material in the production unit of food service industry is similar, and soil removal efficiency all can reach 99.9%, mutually can replace use in actual use for different sorts clean-out system.After test, clean-out system is entered Sewage treatment systems, use clear water to soak 2 hours, clear water is entered Sewage treatment systems, dries equipment stand-by.
Embodiment 11
Selection weight percent is the sodium hydroxide clean-out system of 0.5%, add the sodium lauryl sulphate that weight percent is 0.5,3.0,5.0% respectively, for the cleaning of sugar material in the production unit of tobacco and food service industry, the temperature of clean-out system is respectively 50 DEG C, and the time of clean-out system soaking device is 2 hours.Adopt COD determinator to detect the organic content in clean-out system, initial COD value is C
0, soaking COD value after 2 hours is C
1, extend soak time until COD value is constant, now COD value is C
2.Calculate sugar material soil removal efficiency, concrete data are in table 9.
The calculation formula of sugar material soil removal efficiency is: X
1for=(C
0-C
1)/(C
0-C
2) × 100; Wherein, X
1for washing power, %; C
0for COD value initial in clean-out system, mg/L; C
1for soaking the COD value of clean-out system after 2 hours, mg/L; C
2for soaking certain hour until COD value when the COD value of clean-out system is constant, mg/L.
The tensio-active agent of table 9 Different Weight per-cent is on the impact of sugar material clean effect in production unit
| Tensio-active agent | Concentration (%) | Temperature (DEG C) | Soak time (h) | Soil removal efficiency (%) |
| Sodium lauryl sulphate | 0.5 | 50 | 2 | 93.2 |
| Sodium lauryl sulphate | 3.0 | 50 | 2 | 99.9 |
| Sodium lauryl sulphate | 5.0 | 50 | 2 | 99.9 |
As shown in Table 9, when the weight percent of tensio-active agent-sodium lauryl sulphate is more than 3.0%, clean-out system can reach best effect to sugar material clean effect in production unit, and soil removal efficiency can reach 99.9%.After test, clean-out system is entered Sewage treatment systems, use clear water to soak 2 hours, clear water is entered Sewage treatment systems, dries equipment stand-by.
Embodiment 12
Selection weight percent is the sodium hydroxide clean-out system of 0.5%, add sodium lauryl sulphate, lauryl glucosyl that weight percent is 3.0% respectively, for the cleaning of sugar material in the production unit of tobacco and food service industry, the temperature of clean-out system is respectively 50 DEG C, and the time of clean-out system soaking device is 2 hours.Adopt COD determinator to detect the organic content in clean-out system, initial COD value is C
0, soaking COD value after 2 hours is C
1, extend soak time until COD value is constant, now COD value is C
2.Calculate sugar material soil removal efficiency, concrete data are in table 10.
The calculation formula of sugar material soil removal efficiency is: X
1for=(C
0-C
1)/(C
0-C
2) × 100; Wherein, X
1for washing power, %; C
0for COD value initial in clean-out system, mg/L; C
1for soaking the COD value of clean-out system after 2 hours, mg/L; C
2for soaking certain hour until COD value when the COD value of clean-out system is constant, mg/L.
Table 10 different sorts tensio-active agent is on the impact of sugar material clean effect in production unit
| Tensio-active agent | Concentration (%) | Temperature (DEG C) | Soak time (h) | Soil removal efficiency (%) |
| Sodium lauryl sulphate | 3.0 | 50 | 2 | 99.9 |
| Lauryl glucosyl | 3.0 | 50 | 2 | 99.9 |
As shown in Table 10, under the same conditions, the clean effect removing tobacco residual with sugar material in the production unit of food service industry is similar, and soil removal efficiency all can reach 99.9%, mutually can replace use in actual use for different sorts tensio-active agent.After test, clean-out system is entered Sewage treatment systems, use clear water to soak 2 hours, clear water is entered Sewage treatment systems, dries equipment stand-by.
Above-described embodiment is illustrative principle of the present invention and effect thereof only, but not for limiting the present invention.Any person skilled in the art scholar all without prejudice under spirit of the present invention and category, can modify above-described embodiment or changes.Therefore, such as have in art usually know the knowledgeable do not depart from complete under disclosed spirit and technological thought all equivalence modify or change, must be contained by claim of the present invention.
Claims (9)
1. for clean tobacco and food service industry production unit in the sugar material clean-out system of residual sugar material, it is characterized in that, described sugar
Material clean-out system is aqueous cleaning agent, by weight percentage, comprises following component:
Alkali inorganic substance 0.1-5.0%;
Tensio-active agent 0.5-5.0%;
Water 90.0-99.4%.
2. sugar material clean-out system according to claim 1, it is characterized in that, described alkali inorganic substance is selected from the one in sodium hydroxide, sodium acetate, sodium carbonate, clorox; Described water is distilled water.
3. sugar material clean-out system according to claim 1, it is characterized in that, described tensio-active agent is selected from the one in sodium lauryl sulphate and lauryl glucosyl.
4. according to the preparation method of the arbitrary described sugar material clean-out system of claim 1-3, comprise the following steps: by alkali inorganic substance and surfactant dissolves in water, stir.
5. according to the purposes of the arbitrary described sugar material clean-out system of claim 1-3 residual sugar material in the production unit cleaning tobacco and food service industry.
6., according to the purging method of the sugar material clean-out system of residual sugar material in the arbitrary described a kind of production unit for cleaning tobacco and food service industry of claim 1-4, comprise the following steps:
1), after the sugar material clean-out system prepared being heated, inject production unit, production unit is soaked;
2), after soaking, clean-out system is entered Sewage treatment systems;
3) after being soaked by production unit clear water again, clear water is entered Sewage treatment systems, finally equipment is dried and can put into production again.
7. according to claim 6 sugar material clean-out system purging method, it is characterized in that, as step 1) as described in sugar material clean-out system Heating temperature be 20-70 DEG C.
8. according to claim 6 sugar material clean-out system purging method, it is characterized in that, as step 1) as described in sugar material clean-out system be 0.5-12 hour to the time that production unit soaks.
9. according to claim 6 sugar material clean-out system purging method, it is characterized in that, as step 3) as described in clear water be 0.5-5 hour to the time that production unit soaks.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410440101.0A CN104232343A (en) | 2014-09-01 | 2014-09-01 | Sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries and application thereof |
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|---|---|---|---|
| CN201410440101.0A CN104232343A (en) | 2014-09-01 | 2014-09-01 | Sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries and application thereof |
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| CN104232343A true CN104232343A (en) | 2014-12-24 |
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| CN201410440101.0A Pending CN104232343A (en) | 2014-09-01 | 2014-09-01 | Sugar material cleaning agent for cleaning residual sugar materials in production equipment of tobacco and food industries and application thereof |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110272781A (en) * | 2019-05-05 | 2019-09-24 | 贵州中烟工业有限责任公司 | A kind of cigarette quick-fried pearl cleaning agent and its application method |
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| CN110272781A (en) * | 2019-05-05 | 2019-09-24 | 贵州中烟工业有限责任公司 | A kind of cigarette quick-fried pearl cleaning agent and its application method |
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Application publication date: 20141224 |