CN113616838A - Sterilization deodorant - Google Patents
Sterilization deodorant Download PDFInfo
- Publication number
- CN113616838A CN113616838A CN202111016781.XA CN202111016781A CN113616838A CN 113616838 A CN113616838 A CN 113616838A CN 202111016781 A CN202111016781 A CN 202111016781A CN 113616838 A CN113616838 A CN 113616838A
- Authority
- CN
- China
- Prior art keywords
- essence
- silver ion
- stabilizer
- chinese medicine
- deodorant
- 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.)
- Withdrawn
Links
Images
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
- A61L9/013—Deodorant compositions containing animal or plant extracts, or vegetable material
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N59/00—Biocides, pest repellants or attractants, or plant growth regulators containing elements or inorganic compounds
- A01N59/16—Heavy metals; Compounds thereof
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N65/00—Biocides, pest repellants or attractants, or plant growth regulators containing material from algae, lichens, bryophyta, multi-cellular fungi or plants, or extracts thereof
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N65/00—Biocides, pest repellants or attractants, or plant growth regulators containing material from algae, lichens, bryophyta, multi-cellular fungi or plants, or extracts thereof
- A01N65/08—Magnoliopsida [dicotyledons]
- A01N65/34—Rosaceae [Rose family], e.g. strawberry, hawthorn, plum, cherry, peach, apricot or almond
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2101/00—Chemical composition of materials used in disinfecting, sterilising or deodorising
- A61L2101/32—Organic compounds
- A61L2101/44—Heterocyclic compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
- A61L2209/20—Method-related aspects
- A61L2209/21—Use of chemical compounds for treating air or the like
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Dentistry (AREA)
- Plant Pathology (AREA)
- Environmental Sciences (AREA)
- Wood Science & Technology (AREA)
- Agronomy & Crop Science (AREA)
- Veterinary Medicine (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Mycology (AREA)
- Animal Behavior & Ethology (AREA)
- Epidemiology (AREA)
- Public Health (AREA)
- Natural Medicines & Medicinal Plants (AREA)
- Botany (AREA)
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Pest Control & Pesticides (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
The invention discloses a sterilization deodorant, which consists of the following substances in percentage by weight: 0.7-1.2% of soyabean ethyl sulfate morpholine, 4-8% of dealdehydized alcohol, 0.5-1.5% of beta-cyclodextrin, 0.3-0.7% of silver ion bactericide, 1-3% of shaddock peel, 0.5-1.2% of essence, 1-3% of hawthorn seed particles, 1.5-2.5% of traditional Chinese medicine extract, 1.2-1.8% of stabilizer and 89.1-90% of DI WATER. According to the invention, the added soybean ethyl sulfate morpholine eliminates odor through a bonding effect, and meanwhile, the shaddock peel and essence are heated, so that the odor removing function can be further increased, the odor can be rapidly removed, meanwhile, the added silver ion bactericide and hawthorn kernel particles can be used for efficiently performing sterilization treatment, can be long-acting antibacterial, are nontoxic, tasteless, non-irritant and non-allergic, cannot cause drug resistance of bacteria, and in addition, the traditional Chinese medicine extract is added, so that the protection effect on a human body can be increased.
Description
Technical Field
The invention belongs to the technical field of sterilization deodorant, and particularly relates to a sterilization deodorant.
Background
The sterilization deodorant has no toxic or side effect on human bodies and livestock, is safe to use, has antibacterial, sterilization and deodorization effects, and has good decomposition and removal effects on ammonia, hydrogen sulfide and other malodors.
The existing sterilization deodorant also has some problems: the traditional sterilization deodorant has the advantages that the bad smell is covered by the essence, the bad smell cannot be eliminated, the deodorization effect is poor, meanwhile, during sterilization, bacteria easily generate drug resistance, and long-acting antibiosis is not facilitated, so that the sterilization effect is reduced, and therefore, the sterilization deodorant is provided.
Disclosure of Invention
The invention aims to provide a sterilization deodorant, which solves the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme: a sterilization deodorant consists of the following substances in percentage by weight: 0.7-1.2% of soyabean ethyl sulfate morpholine, 4-8% of dealdehydized alcohol, 0.5-1.5% of beta-cyclodextrin, 0.3-0.7% of silver ion bactericide, 1-3% of shaddock peel, 0.5-1.2% of essence, 1-3% of hawthorn seed particles, 1.5-2.5% of traditional Chinese medicine extract, 1.2-1.8% of stabilizer and 89.1-90% of DI WATER.
Preferably, the composition comprises the following substances in percentage by weight: 0.8-1.1% of soyabean ethyl sulfate morpholine, 4.5-7.8% of dealdehydized alcohol, 0.6-1.2% of beta-cyclodextrin, 0.3-0.6% of silver ion bactericide, 1.2-2.8% of shaddock peel, 0.6-1.0% of essence, 1.2-2.8% of hawthorn seed particles, 1.8-2.8% of traditional Chinese medicine extract, 1.4-1.6% of stabilizer and 89.1-89.7% of DI WATER.
Preferably, the composition comprises the following substances in percentage by weight: 0.9-1.1% of soyabean ethyl sulfate morpholine, 9.2-9.6% of dealdehydized alcohol, 0.6-1.2% of beta-cyclodextrin, 0.4-0.6% of silver ion bactericide, 1.2-2.8% of shaddock peel, 0.6-1.0% of essence, 1.2-2.8% of hawthorn seed particles, 1.8-2.8% of traditional Chinese medicine extract, 1.4-1.6% of stabilizer and 89.1-89.5% of DI WATER.
Preferably, the composition comprises the following substances in percentage by weight: 1% of soybean ethyl sulfate morpholine, 9.3% of dealdehydized alcohol, 0.8% of beta-cyclodextrin, 0.5% of silver ion bactericide, 1.6% of shaddock peel, 0.8% of essence, 1.8% of hawthorn seed granules, 2% of traditional Chinese medicine extract, 1.5% of stabilizer and 89.2% of DI WATER.
Preferably, the stabilizer is selected from at least one of diisocyanate, maleic anhydride, boric acid, borax, glutaraldehyde, and persulfate.
Preferably, the preparation process of the sterilizing deodorant comprises the following steps: adding DI WATER into a material preparing pot, adding the soybean ethyl sulfate morpholine, beta-cyclodextrin, shaddock peel, essence, hawthorn seed particles and the traditional Chinese medicine extract into the DI WATER, stirring uniformly, then adding dealdehydized alcohol, stirring uniformly, finally adding the silver ion bactericide and the stabilizer, stopping stirring after stirring uniformly, sampling to be detected, and filling after the inspection is qualified.
Preferably, the stirring speed is 500-1500r/min, and the time of each stirring is 2-4 h.
Preferably, the test process comprises sterilization detection and deodorization detection, wherein the sterilization detection comprises detection of the content of escherichia coli, staphylococcus aureus and candida albicans, and the deodorization detection comprises detection of the content of ammonia and hydrogen sulfide.
Compared with the prior art, the invention has the beneficial effects that: according to the invention, the added soybean ethyl sulfate morpholine eliminates odor through a bonding effect, and meanwhile, the shaddock peel and essence are heated, so that the odor removing function can be further increased, the odor can be rapidly removed, meanwhile, the added silver ion bactericide and hawthorn kernel particles can be used for efficiently performing sterilization treatment, can be long-acting antibacterial, are nontoxic, tasteless, non-irritant and non-allergic, cannot cause drug resistance of bacteria, and in addition, the traditional Chinese medicine extract is added, so that the protection effect on a human body can be increased.
Drawings
FIG. 1 is a process flow diagram of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
The invention provides a technical scheme that: a sterilization deodorant consists of the following substances in percentage by weight: 0.7% of soyabean ethyl sulfate morpholine, 4% of dealdehydized alcohol, 0.5% of beta-cyclodextrin, 0.3% of silver ion bactericide, 1% of shaddock peel, 0.5% of essence, 1% of hawthorn seed particles, 1.5% of traditional Chinese medicine extract, 1.2% of stabilizer and 89.1% of DI WATER.
In this embodiment, preferably, the stabilizer is selected from diisocyanates.
In this embodiment, preferably, the production process of the dealdehydized alcohol is as follows: the method comprises the following steps:
s11, raw material acceptance: selecting grains with starch content of 30 as raw materials, and cleaning with clear water for later use;
s12, impurity removal of raw materials: conveying the cleaned raw materials to a stone remover and an impurity remover through a belt conveyor to remove silt, stones and metal impurities in the raw material grains;
s13, raw material crushing: weighing the raw materials after removing impurities, conveying the raw materials to a hammer mill through a belt conveyor for crushing to obtain raw material powder, wherein in the raw material crushing process, the mesh diameter of a screen mesh used by the hammer mill is 0.8mm, and the crushed raw material powder is 15 meshes;
s14, stirring raw material powder: pouring the crushed raw material powder into a stirring tank, adding process water, distilled residual water, CaCl2 and high-temperature-resistant alpha-amylase into the stirring tank, and uniformly stirring; the ratio of the raw material powder, the process water, the distilled residual water, the CaCl2 and the high-temperature-resistant alpha-amylase is 2:7:0.5:0.25: 0.25;
s15, precooking and puffing: feeding the stirred material obtained in the step S14 into a liquefaction tank, heating to 95 ℃ under the pressure of 150Pa, and liquefying for 2 hours to obtain liquefied mash;
s16, saccharification: sending the liquefied mash to a saccharification tank, adding 50% of vinasse centrifugal liquid into the liquefied mash to reduce the pH value of the liquefied mash to 4.5, cooling to 60 ℃ by a spiral plate heat exchanger, adding saccharifying enzyme into the saccharification tank, immediately cooling to 30 ℃ by the spiral plate heat exchanger to obtain the saccharified mash, wherein the DE value of the saccharified mash is 2%;
s17, fermentation: cooling the saccharified mash to a fermentation temperature of 29 ℃ by a spray cooler, inoculating dry yeast with the saccharified mash amount of 9% by taking immobilized yeast as a carrier, uniformly mixing, fermenting for 55h, and adding carbendazim to sterilize the fermented mash in the fermentation process so as to prevent the growth of microorganisms;
s18, distillation: feeding the fermented mash into a distillation tower with a set temperature of 75 ℃, simultaneously adding 9% by mass of sodium hydroxide, distilling for 18min, purifying alcohol in the mash, circularly distilling the alcohol which does not reach the concentration index, and discharging vinasse and alcohol wastewater from a vinasse groove;
s19, cooling: and cooling the alcohol extracted from the distillation tower to normal temperature by a plate cooler to obtain the dealdehydized alcohol.
In this embodiment, preferably, the raw potatoes selected in S11 are cassava, sweet potatoes, potatoes and yams, the water content of the raw materials is 8%, the metal removed in the impurity removal process of the raw materials in S12 is iron, and the used impurity remover removes iron electromagnetically.
In this embodiment, preferably, after the alcohol wastewater in S18 is discharged, the wastewater needs to be treated by the following steps: step one, removing larger impurities from the alcohol wastewater through a grid, and then, allowing the alcohol wastewater to enter an adjusting tank to effectively adjust the water quantity and the water quality; step two, lifting the mixture into a primary sedimentation tank by using a pump for pretreatment, adding an alcohol wastewater treatment agent into the primary sedimentation tank at the stage, uniformly mixing the alcohol wastewater treatment agent and the alcohol wastewater treatment agent, and standing for 35 min; and step three, the wastewater treated in the step three enters a hydrolysis acidification tank and a contact oxidation tank for biochemical treatment, the effluent enters a secondary sedimentation tank for mud-water separation, one part of sludge in the secondary sedimentation tank flows back to the front of an aerobic tank, and the other part of sludge is discharged to a sludge tank.
In this embodiment, preferably, the production process of the silver ion bactericide mainly includes the steps of: taking raw material silver and fruit acid, processing the raw material silver into analytically pure silver, then adding the fruit acid, heating and stirring, then filtering the silver ion solution, detecting, and packaging the stock solution finished product to obtain the silver ion bactericide.
In this embodiment, preferably, the DI WATER is prepared by using reverse osmosis-ion exchange equipment, and the basic process flow is as follows: raw water, a multi-media filter, an activated carbon filter, a precision filter, reverse osmosis equipment, a mixed bed, an ultra-pure water tank, an ultra-pure water pump, a post cartridge filter and deionized water.
In this embodiment, preferably, the preparation process of the sterilizing deodorant is as follows: adding DI WATER into a material preparing pot, adding the soybean ethyl sulfate morpholine, beta-cyclodextrin, shaddock peel, essence, hawthorn seed particles and the traditional Chinese medicine extract into the DI WATER, stirring uniformly, then adding dealdehydized alcohol, stirring uniformly, finally adding the silver ion bactericide and the stabilizer, stopping stirring after stirring uniformly, sampling to be detected, and filling after the inspection is qualified.
In this embodiment, the stirring speed is preferably 500r/min, and the time for each stirring is preferably 4 h.
Example 2
The invention provides a technical scheme that: a sterilization deodorant consists of the following substances in percentage by weight: 1.2% of soyabean ethyl sulfate morpholine, 8% of dealdehydized alcohol, 1.5% of beta-cyclodextrin, 0.7% of silver ion bactericide, 3% of shaddock peel, 1.2% of essence, 3% of hawthorn seed particles, 2.5% of traditional Chinese medicine extract, 1.8% of stabilizer and 90% of DI WATER.
In this embodiment, preferably, the production process of the dealdehydized alcohol is as follows: the method comprises the following steps:
s11, raw material acceptance: selecting grains with starch content of 40% as raw materials, and cleaning with clear water for later use;
s12, impurity removal of raw materials: conveying the cleaned raw materials to a stone remover and an impurity remover through a belt conveyor to remove silt, stones and metal impurities in the raw material grains;
s13, raw material crushing: weighing the raw materials after removing impurities, conveying the raw materials to a hammer mill through a belt conveyor for crushing to obtain raw material powder, wherein in the raw material crushing process, the mesh diameter of a screen mesh used by the hammer mill is 1.6mm, and the crushed raw material powder is 45 meshes;
s14, stirring raw material powder: pouring the crushed raw material powder into a stirring tank, adding process water, distilled residual water, CaCl2 and high-temperature-resistant alpha-amylase into the stirring tank, and uniformly stirring; the ratio of the raw material powder, the process water, the distilled residual water, the CaCl2 and the high-temperature-resistant alpha-amylase is 2:7:0.5:0.25: 0.25;
s15, precooking and puffing: feeding the stirred material obtained in the step S14 into a liquefaction tank, heating to 95 ℃ under the pressure of 150Pa, and liquefying for 2 hours to obtain liquefied mash;
s16, saccharification: sending the liquefied mash to a saccharification tank, adding 50% of vinasse centrifugal liquid into the liquefied mash to reduce the pH value of the liquefied mash to 4.5, cooling to 60 ℃ by a spiral plate heat exchanger, adding saccharifying enzyme into the saccharification tank, immediately cooling to 30 ℃ by the spiral plate heat exchanger to obtain the saccharified mash, wherein the DE value of the saccharified mash is 3%;
s17, fermentation: cooling the saccharified mash to a fermentation temperature of 34 ℃ by a spray cooler, inoculating dry yeast with 16% of the saccharified mash by taking immobilized yeast as a carrier, uniformly mixing, fermenting for 85h, and adding carbendazim to sterilize the fermented mash in the fermentation process so as to prevent the growth of microorganisms;
s18, distillation: feeding the fermented mash into a distillation tower with a set temperature of 90 ℃, simultaneously adding 21% by mass of sodium hydroxide, distilling for 32min, purifying alcohol in the mash, circularly distilling the alcohol which does not reach the concentration index, and discharging vinasse and alcohol wastewater from a vinasse groove;
s19, cooling: and cooling the alcohol extracted from the distillation tower to normal temperature by a plate cooler to obtain the dealdehydized alcohol.
In this embodiment, preferably, the raw potatoes selected in S11 are cassava, sweet potatoes, potatoes and yams, the water content of the raw materials is 15%, the metal removed in the impurity removal process of the raw materials in S12 is iron, and the used impurity remover removes iron electromagnetically.
In this embodiment, preferably, after the alcohol wastewater in S18 is discharged, the wastewater needs to be treated by the following steps: step one, removing larger impurities from the alcohol wastewater through a grid, and then, allowing the alcohol wastewater to enter an adjusting tank to effectively adjust the water quantity and the water quality; step two, lifting the mixture into a primary sedimentation tank by using a pump for pretreatment, adding an alcohol wastewater treatment agent into the primary sedimentation tank at the stage, uniformly mixing the alcohol wastewater treatment agent and the alcohol wastewater treatment agent, and standing for 45 min; and step three, the wastewater treated in the step three enters a hydrolysis acidification tank and a contact oxidation tank for biochemical treatment, the effluent enters a secondary sedimentation tank for mud-water separation, one part of sludge in the secondary sedimentation tank flows back to the front of an aerobic tank, and the other part of sludge is discharged to a sludge tank.
In this embodiment, preferably, the production process of the silver ion bactericide mainly includes the steps of: taking raw material silver and fruit acid, processing the raw material silver into analytically pure silver, then adding the fruit acid, heating and stirring, then filtering the silver ion solution, detecting, and packaging the stock solution finished product to obtain the silver ion bactericide.
In this embodiment, preferably, the DI WATER is prepared by matching reverse osmosis equipment and electrodeionization equipment, and the basic process flow is as follows: raw water, a multi-medium filter, an activated carbon filter, a precision filter, a reverse osmosis device, electric deionization, an ultra-pure water tank, an ultra-pure water pump, a post cartridge filter and deionized water.
In this embodiment, preferably, the preparation process of the sterilizing deodorant is as follows: adding DI WATER into a material preparing pot, adding the soybean ethyl sulfate morpholine, beta-cyclodextrin, shaddock peel, essence, hawthorn seed particles and the traditional Chinese medicine extract into the DI WATER, stirring uniformly, then adding dealdehydized alcohol, stirring uniformly, finally adding the silver ion bactericide and the stabilizer, stopping stirring after stirring uniformly, sampling to be detected, and filling after the inspection is qualified.
In this embodiment, the stirring speed is 1500r/min, and the time for each stirring is preferably 2 h.
Example 3
The invention provides a technical scheme that: a sterilization deodorant consists of the following substances in percentage by weight: 1% of soybean ethyl sulfate morpholine, 9.3% of dealdehydized alcohol, 0.8% of beta-cyclodextrin, 0.5% of silver ion bactericide, 1.6% of shaddock peel, 0.8% of essence, 1.8% of hawthorn seed granules, 2% of traditional Chinese medicine extract, 1.5% of stabilizer and 89.2% of DI WATER.
In this embodiment, preferably, the production process of the dealdehydized alcohol is as follows: the method comprises the following steps:
s11, raw material acceptance: selecting grains with starch content of 30 as raw materials, and cleaning with clear water for later use;
s12, impurity removal of raw materials: conveying the cleaned raw materials to a stone remover and an impurity remover through a belt conveyor to remove silt, stones and metal impurities in the raw material grains;
s13, raw material crushing: weighing the raw materials after removing impurities, conveying the raw materials to a hammer mill through a belt conveyor for crushing to obtain raw material powder, wherein in the raw material crushing process, the mesh diameter of a screen mesh used by the hammer mill is 0.8mm, and the crushed raw material powder is 15 meshes;
s14, stirring raw material powder: pouring the crushed raw material powder into a stirring tank, adding process water, distilled residual water, CaCl2 and high-temperature-resistant alpha-amylase into the stirring tank, and uniformly stirring; the ratio of the raw material powder, the process water, the distilled residual water, the CaCl2 and the high-temperature-resistant alpha-amylase is 2:7:0.5:0.25: 0.25;
s15, precooking and puffing: feeding the stirred material obtained in the step S14 into a liquefaction tank, heating to 95 ℃ under the pressure of 150Pa, and liquefying for 2 hours to obtain liquefied mash;
s16, saccharification: sending the liquefied mash to a saccharification tank, adding 50% of vinasse centrifugal liquid into the liquefied mash to reduce the pH value of the liquefied mash to 4.5, cooling to 60 ℃ by a spiral plate heat exchanger, adding saccharifying enzyme into the saccharification tank, immediately cooling to 30 ℃ by the spiral plate heat exchanger to obtain the saccharified mash, wherein the DE value of the saccharified mash is 2%;
s17, fermentation: cooling the saccharified mash to a fermentation temperature of 29 ℃ by a spray cooler, inoculating dry yeast with the saccharified mash amount of 9% by taking immobilized yeast as a carrier, uniformly mixing, fermenting for 55h, and adding carbendazim to sterilize the fermented mash in the fermentation process so as to prevent the growth of microorganisms;
s18, distillation: feeding the fermented mash into a distillation tower with a set temperature of 75 ℃, simultaneously adding 9% by mass of sodium hydroxide, distilling for 18min, purifying alcohol in the mash, circularly distilling the alcohol which does not reach the concentration index, and discharging vinasse and alcohol wastewater from a vinasse groove;
s19, cooling: and cooling the alcohol extracted from the distillation tower to normal temperature by a plate cooler to obtain the dealdehydized alcohol.
In this embodiment, preferably, after the alcohol wastewater in S18 is discharged, the wastewater needs to be treated by the following steps: step one, removing larger impurities from the alcohol wastewater through a grid, and then, allowing the alcohol wastewater to enter an adjusting tank to effectively adjust the water quantity and the water quality; step two, lifting the mixture into a primary sedimentation tank by using a pump for pretreatment, adding an alcohol wastewater treatment agent into the primary sedimentation tank at the stage, uniformly mixing the alcohol wastewater treatment agent and the alcohol wastewater treatment agent, and standing for 35 min; and step three, the wastewater treated in the step three enters a hydrolysis acidification tank and a contact oxidation tank for biochemical treatment, the effluent enters a secondary sedimentation tank for mud-water separation, one part of sludge in the secondary sedimentation tank flows back to the front of an aerobic tank, and the other part of sludge is discharged to a sludge tank.
In this embodiment, preferably, the production process of the silver ion bactericide mainly includes the steps of: taking raw material silver and fruit acid, processing the raw material silver into analytically pure silver, then adding the fruit acid, heating and stirring, then filtering the silver ion solution, detecting, and packaging the stock solution finished product to obtain the silver ion bactericide.
In this embodiment, preferably, the DI WATER is prepared by using reverse osmosis-ion exchange equipment, and the basic process flow is as follows: raw water, a multi-media filter, an activated carbon filter, a precision filter, reverse osmosis equipment, a mixed bed, an ultra-pure water tank, an ultra-pure water pump, a post cartridge filter and deionized water.
In this embodiment, preferably, the preparation process of the sterilizing deodorant is as follows: adding DI WATER into a material preparing pot, adding the soybean ethyl sulfate morpholine, beta-cyclodextrin, shaddock peel, essence, hawthorn seed particles and the traditional Chinese medicine extract into the DI WATER, stirring uniformly, then adding dealdehydized alcohol, stirring uniformly, finally adding the silver ion bactericide and the stabilizer, stopping stirring after stirring uniformly, sampling to be detected, and filling after the inspection is qualified.
The invention has the advantages that: according to the invention, the added soybean ethyl sulfate morpholine eliminates odor through a bonding effect, and meanwhile, the shaddock peel and essence are heated, so that the odor removing function can be further increased, the odor can be rapidly removed, meanwhile, the added silver ion bactericide and hawthorn kernel particles can be used for efficiently performing sterilization treatment, can be long-acting antibacterial, are nontoxic, tasteless, non-irritant and non-allergic, cannot cause drug resistance of bacteria, and in addition, the traditional Chinese medicine extract is added, so that the protection effect on a human body can be increased.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (8)
1. A sterilization deodorant is characterized in that: the composition comprises the following substances in percentage by weight: 0.7-1.2% of soyabean ethyl sulfate morpholine, 4-8% of dealdehydized alcohol, 0.5-1.5% of beta-cyclodextrin, 0.3-0.7% of silver ion bactericide, 1-3% of shaddock peel, 0.5-1.2% of essence, 1-3% of hawthorn seed particles, 1.5-2.5% of traditional Chinese medicine extract, 1.2-1.8% of stabilizer and 89.1-90% of DIWATER.
2. A bactericidal deodorant as set forth in claim 1, wherein: the composition comprises the following substances in percentage by weight: 0.8-1.1% of soyabean ethyl sulfate morpholine, 4.5-7.8% of dealdehydized alcohol, 0.6-1.2% of beta-cyclodextrin, 0.3-0.6% of silver ion bactericide, 1.2-2.8% of shaddock peel, 0.6-1.0% of essence, 1.2-2.8% of hawthorn seed particles, 1.8-2.8% of traditional Chinese medicine extract, 1.4-1.6% of stabilizer and 89.1-89.7% of DIWATER.
3. A bactericidal deodorant as set forth in claim 2, wherein: the composition comprises the following substances in percentage by weight: 0.9-1.1% of soyabean ethyl sulfate morpholine, 9.2-9.6% of dealdehydized alcohol, 0.6-1.2% of beta-cyclodextrin, 0.4-0.6% of silver ion bactericide, 1.2-2.8% of shaddock peel, 0.6-1.0% of essence, 1.2-2.8% of hawthorn seed particles, 1.8-2.8% of traditional Chinese medicine extract, 1.4-1.6% of stabilizer and 89.1-89.5% of DIWATER.
4. A bactericidal deodorant as set forth in claim 3, wherein: the composition comprises the following substances in percentage by weight: 1% of soyabean ethyl sulfate morpholine, 9.3% of dealdehydized alcohol, 0.8% of beta-cyclodextrin, 0.5% of silver ion bactericide, 1.6% of shaddock peel, 0.8% of essence, 1.8% of hawthorn seed granules, 2% of traditional Chinese medicine extract, 1.5% of stabilizer and 89.2% of DIWATER.
5. A bactericidal deodorant as set forth in claim 1, wherein: the stabilizer is at least one selected from diisocyanate, maleic anhydride, boric acid, borax, glutaraldehyde and persulfate.
6. The sterilizing deodorant according to claim 1, wherein the sterilizing deodorant is prepared by the following process: adding DIWATER into a material preparing pot, adding the soyabean ethyl sulfate morpholine, beta-cyclodextrin, shaddock peel, essence, hawthorn seed particles and the traditional Chinese medicine extract into the DIWATER, uniformly stirring, then adding dealdehydized alcohol, uniformly stirring, finally adding the silver ion bactericide and the stabilizer, stopping stirring after uniformly stirring, sampling to be detected, and filling after the inspection is qualified.
7. The bactericidal deodorant as set forth in claim 5, wherein: the stirring speed is 500-1500r/min, and the stirring time is 2-4 h.
8. The bactericidal deodorant as set forth in claim 6, wherein: the detection process comprises sterilization detection and deodorization detection, wherein the sterilization detection comprises the detection of the content of escherichia coli, staphylococcus aureus and candida albicans, and the deodorization detection comprises the detection of the content of ammonia and hydrogen sulfide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111016781.XA CN113616838A (en) | 2021-08-31 | 2021-08-31 | Sterilization deodorant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111016781.XA CN113616838A (en) | 2021-08-31 | 2021-08-31 | Sterilization deodorant |
Publications (1)
Publication Number | Publication Date |
---|---|
CN113616838A true CN113616838A (en) | 2021-11-09 |
Family
ID=78388733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202111016781.XA Withdrawn CN113616838A (en) | 2021-08-31 | 2021-08-31 | Sterilization deodorant |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113616838A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114916562A (en) * | 2022-06-06 | 2022-08-19 | 山西世纪超蓝科技有限公司 | Plant type sterilization deodorant and preparation method thereof |
-
2021
- 2021-08-31 CN CN202111016781.XA patent/CN113616838A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114916562A (en) * | 2022-06-06 | 2022-08-19 | 山西世纪超蓝科技有限公司 | Plant type sterilization deodorant and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101659681B (en) | Method for producing wood sugar product | |
CN101665523B (en) | The production method of L-arabinose and D-xylose pref | |
CN101475286B (en) | Sewage treatment method for stevioside production line | |
AU2010228843B2 (en) | Method for producing clarified juice, packagible juice, ethanol and sugar from sugarcane and system thereof | |
CN103525870A (en) | Microbial flocculant as well as preparation method and application thereof | |
CN101696379A (en) | Method for producing distilled spirit | |
CN108203165A (en) | A kind of complex enzyme biochemical water purification agent and preparation method thereof | |
CN113616838A (en) | Sterilization deodorant | |
CN101665524B (en) | Method for producing L-arabinose | |
CN105217803B (en) | A kind of sewage disposal is with bacillus accelerator and preparation method thereof | |
CN113200613A (en) | Microbial nutrient solution for sewage treatment and preparation method and application thereof | |
CN102219286A (en) | Treatment method of wastewater generated during citric acid preparation and preparation method of citric acid | |
CN101157499A (en) | Plant straw treating organic sewage comprehensive utilization method | |
CN103387313A (en) | Method for treating cellulosic ethanol waste water | |
CN211056982U (en) | Biogas slurry resource utilization system device | |
US20050023214A1 (en) | Seaweed-based product for treating liquid waste, together with method for making and using the seaweed-based product | |
CN110182948B (en) | Biological sewage treatment method based on activated sludge fermentation product | |
CN111252997A (en) | Treatment method of betaine production wastewater | |
CN111252996A (en) | Treatment method of betaine production wastewater | |
Conradie | Influence of winemaking practices on the chemical characteristics of winery wastewater and the water usages of wineries. | |
CN109022504B (en) | Method for producing citric acid by treating anaerobic digestion solution through electrodialysis | |
CN108650918A (en) | The method for improveing soil using composite enzyme | |
CN108585219A (en) | Utilize the method for composite enzyme treated sewage | |
CN1462799A (en) | Technique of preparing fermentation culture medium for microbe | |
JPH0466639B2 (en) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20211109 |
|
WW01 | Invention patent application withdrawn after publication |