CN202760063U - Novel ammonia phenol production device - Google Patents
Novel ammonia phenol production device Download PDFInfo
- Publication number
- CN202760063U CN202760063U CN201220283424XU CN201220283424U CN202760063U CN 202760063 U CN202760063 U CN 202760063U CN 201220283424X U CN201220283424X U CN 201220283424XU CN 201220283424 U CN201220283424 U CN 201220283424U CN 202760063 U CN202760063 U CN 202760063U
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- tank
- agitator tank
- batcher
- ethanol
- centrifugal pump
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- Expired - Fee Related
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- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The utility model discloses a novel ammonia phenol production device, and belongs to the field of disinfectors. The device comprises an ethanol oxidation tank, a first agitation tank, a second agitation tank, a first proportioning tank, a second proportioning tank and a double-end liquid quantificational filling machine, takes ethanol, oxygen, catalyst, tricresol, dodecylbenzene sulfonic acid, an emulsifier, an oxidizer and a stabilizing agent as raw materials, and produces ammonia phenol through the processes of preparation of acetic acid, step mixing of ingredient, subpackage of finished products and the like. The device adopting the technological process has the main advantages that general equipment is utilized, the process is simple, the product quality is good, toxic or harmful gases and liquid are not discharged, an efficient, high-speed and economical disinfector with stable performances can be produced, and the disinfector can rapidly kill various germs, viruses, funguses and spores and particularly has special efficiency on swine foot and mouth disease.
Description
Technical field
The utility model belongs to the disinfectant field, relates in particular to a kind of mechanical device of producing peace phenol.
Background technology
Peace phenol; have another name called compound phenol; outward appearance is dark red brown viscous fluid; special smell is arranged; peace phenol is with three cresols; acetic acid; DBSA is the formulated water soluble mixt of primary raw material; peace phenol can damage the somatic cells film; it also is protein denaturant during higher concentration; so bactericidal action is arranged; passing through in addition anti-bacteria dehydrase and oxidase isoreactivity, and produce bacteriostasis, is a kind of Cidex-7; can kill various bacteria and virus; because having adopted the composite emulsifying technology, the drop of medicine disperses very thin (diameter is in the 0.1-100um scope), fast automatic diffusion when water-soluble; can form uniform milky white solution; solution is sprayed onto when being sterilized the thing surface and forms layer protecting film simultaneously, makes medicine can be adsorbed quickly and bring into play bactericidal action, thereby improves biocidal efficacies; effectively sterilizing time was to keep the longest disinfectant of disinfection effect after rare solution for 7 days.Peace phenol has added surfactant, stabilizing agent, oxidant when preparation, make it to sterilised object preferably moistening and cleaning action be arranged, and effectively guarantees simultaneously precipitation and the phenomenon of becoming sour can not occur by disinfectant steady quality within the shelf-life.Peace phenol has the effects such as the insect such as the fly of killing, mosquito, spider, ant, earthworm, protozoon and egg capsule, and multiple parasitic ovum is also had killing action, can also suppress growing of the insect such as mosquito, fly and the plague of rats; Be adapted to the sterilization of aphthovirus, avian influenza virus, swine fever, blue otopathy, oedema, haemophilus, Escherichia coli, the disease of breathing, PCV-II, newcastle disease virus, coronavirus, multiple mould, coccidia, insect etc.; Especially the infection pathogeny of respiratory tract had splendid dissipation effect.Can be widely used in disinfection in the cultivation closed environment, the aqueous solution that is made into 0.3%-1% during use sprays, and also can be made into 1.6% aqueous solution soaking.The utility model is a kind of mechanical device of producing peace phenol, this device is with the oxidation of ethanol tank, the first agitator tank, the second agitator tank, the first batcher, the second batcher, the Bipitch liquid dosing filling machine is equipment, with ethanol, oxygen, catalyzer, three cresols, DBSA, emulsifier, oxidant, stabilizing agent is raw material, by producing of acetic acid, the substep blending of batching, the operations such as the packing of finished product are produced peace phenol, the major advantage of this technological process is: use common apparatus, technique is simple, good product quality, without toxic and harmful and fluid discharge, can produce efficient, quick-acting, stable in properties, economical disinfectant, this disinfectant can be killed all kinds of germs fast, virus, fungi, gemma particularly has special efficacy to No. five diseases of pig.
Summary of the invention
The problem that the utility model mainly solves provides a kind of mechanical device of suitability for industrialized production peace phenol, this device is comprised of oxidation of ethanol tank, the first agitator tank, the second agitator tank, the first batcher, the second batcher, Bipitch liquid dosing filling machine, produce peace phenol take ethanol, three cresols, DBSA as primary raw material, its advantage is: use common apparatus, simple, the good quality of product of technique, can produce efficient, quick-acting, stable in properties, economical disinfectant.
The technical solution adopted in the utility model is:
A kind of novel peace phenol process units comprises: oxidation of ethanol tank 1, the first agitator tank 2, the second agitator tank 3, the first batcher 4, the second batcher 5, Bipitch liquid dosing filling machine 6; Oxidation of ethanol tank 1 is provided with ethanol import 7, catalyst inlet 8, oxygen inlet 9,2 of oxidation of ethanol tank 1 to first agitator tanks are provided with centrifugal pump and pipeline 10, the first agitator tank 2 is provided with three cresols imports 11,3 of the first agitator tank 2 to second agitator tanks are provided with centrifugal pump and pipeline 12, the first batcher 4 is provided with water inlet 13, DBSA import 14,3 of the first batcher 4 to second agitator tanks are provided with centrifugal pump and pipeline 15, the second batcher 5 is provided with water inlet 16, emulsifier import 17, oxidant inlet 18, stabilizing agent import 19,3 of the second batcher 5 to second agitator tanks are provided with centrifugal pump and pipeline 20, the second agitator tank 3 is provided with centrifugal pump and pipeline 21 to 6 of Bipitch liquid dosing filling machines, and Bipitch liquid dosing filling machine 6 is provided with product outlet 22.
Further technical scheme of the present utility model is:
Described whole centrifugal pump is stainless steel centrifugal pump;
Described whole pipeline is polyethylene pipe.
The beneficial effects of the utility model are: a kind of novel peace phenol process units is provided, the advantage of this process units is: use common apparatus, simple, the good product quality of technique, without toxic and harmful and fluid discharge, can produce efficient, quick-acting, stable in properties, economical disinfectant, this disinfectant can be killed all kinds of germs, virus, fungi, gemma fast, particularly No. five diseases of pig is had special efficacy.
Description of drawings:
Be the utility model principle schematic such as Fig. 1.
Embodiment
Further specify the particular content that uses this new device production peace phenol most preferred embodiment below in conjunction with accompanying drawing:
With quantitative ethanol by be arranged at the ethanol import 7 on the oxidation of ethanol tank 1, quantitative catalyzer is sent into oxidation of ethanol tank 1 by catalyst inlet 8, quantitative oxygen by oxygen inlet 9, make while stirring ethanol generation oxidation reaction, generate the aqueous solution of acetic acid.
2. aqueous acetic acid is sent into the first agitator tank 2 by the centrifugal pump and the pipeline 10 that are arranged at 2 of oxidation of ethanol tank 1 and the first agitator tanks, by the three cresols imports 11 that are arranged on the first agitator tank 2 three quantitative cresols are sent into the first agitator tank 2, send into the second agitator tank 3 by the centrifugal pump and the pipeline 12 that are arranged at 3 of the first agitator tank 2 and the second agitator tanks after the blending evenly.
3. quantitative water is sent into the first batcher 4 by the water inlet 13 that is arranged on the first batcher 4, quantitative DBSA is sent into the first batcher 4 by the DBSA import 14 that is arranged on the first batcher 4, sends into the second agitator tank 3 by the centrifugal pump and the pipeline 15 that are arranged at 3 of the first batcher 4 and the second agitator tanks after the blending evenly under the normal temperature.
4. quantitative water is sent into the second batcher 5 by the water inlet 16 that is arranged on the second batcher 5, temperature in the second batcher 5 is elevated to 45 ℃, respectively quantitative emulsifier, oxidant, stabilizing agent are sent into the second batcher 5 by the emulsifier import 17, oxidant inlet 18, the stabilizing agent import 19 that are arranged on the second batcher 5, sent into the second agitator tank 3 by the centrifugal pump and the pipeline 20 that are arranged at 3 of the second batcher 5 and the second agitator tanks after the blending evenly.
5. the centrifugal pump by being arranged at 6 of the second agitator tank 3 and Bipitch liquid dosing filling machines and pipeline 21 after all material blending in the second agitator tank 3 are evenly sent into Bipitch liquid dosing filling machine 6 and carry out can, finished product is from being arranged at product outlet 22 dischargings on the Bipitch liquid dosing filling machine 6, and can is to obtain finished product after 500 milliliters/bottle, 1000 milliliters/bottle, 5000 milliliters/bottle.
Claims (3)
1. a novel peace phenol process units is characterized in that: comprise oxidation of ethanol tank (1), the first agitator tank (2), the second agitator tank (3), the first batcher (4), the second batcher (5), Bipitch liquid dosing filling machine (6); Oxidation of ethanol tank (1) is provided with ethanol import (7), catalyst inlet (8), oxygen inlet (9), oxidation of ethanol tank (1) is to being provided with centrifugal pump and pipeline (10) between the first agitator tank (2), the first agitator tank (2) is provided with three cresols and enters (11), the first agitator tank (2) is to being provided with centrifugal pump and pipeline (12) between the second agitator tank (3), the first batcher (4) is provided with water inlet (13), DBSA import (14), the first batcher (4) is to being provided with centrifugal pump and pipeline (15) between the second agitator tank (3), the second batcher (5) is provided with water inlet (16), emulsifier import (17), oxidant inlet (18), stabilizing agent import (19), the second batcher (5) is to being provided with centrifugal pump and pipeline (20) between the second agitator tank (3), the second agitator tank (3) is to being provided with centrifugal pump and pipeline (21) between Bipitch liquid dosing filling machine (6), Bipitch liquid dosing filling machine (6) is provided with product outlet (22).
2. a kind of novel peace phenol process units according to claim 1, it is characterized in that: described whole centrifugal pumps are stainless steel centrifugal pump.
3. a kind of novel peace phenol process units according to claim 1, it is characterized in that: described whole pipelines are polyethylene pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220283424XU CN202760063U (en) | 2012-06-16 | 2012-06-16 | Novel ammonia phenol production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220283424XU CN202760063U (en) | 2012-06-16 | 2012-06-16 | Novel ammonia phenol production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202760063U true CN202760063U (en) | 2013-03-06 |
Family
ID=47766682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220283424XU Expired - Fee Related CN202760063U (en) | 2012-06-16 | 2012-06-16 | Novel ammonia phenol production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202760063U (en) |
-
2012
- 2012-06-16 CN CN201220283424XU patent/CN202760063U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130306 Termination date: 20130616 |