CN205576116U - Take carbon dioxide processing apparatus's fermentation cylinder - Google Patents
Take carbon dioxide processing apparatus's fermentation cylinder Download PDFInfo
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- CN205576116U CN205576116U CN201620380694.0U CN201620380694U CN205576116U CN 205576116 U CN205576116 U CN 205576116U CN 201620380694 U CN201620380694 U CN 201620380694U CN 205576116 U CN205576116 U CN 205576116U
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Abstract
The utility model discloses a take carbon dioxide processing apparatus's fermentation cylinder, including a jar body, agitating unit and music device, jar body upper portion is equipped with the charge door, and a jar body lower part is equipped with the discharge gate, and the discharge gate is connected with ejection of compact pipeline, is equipped with the bleeder valve on this ejection of compact pipeline, jar body upper portion is equipped with the gas vent, is connected with exhaust duct on the gas vent, is equipped with discharge valve on this exhaust duct, exhaust duct's exit end is connected with carbon dioxide compressor arrangement, and carbon dioxide compressor arrangement's both sides are equipped with carbon dioxide feed inlet and carbon dioxide discharge gate respectively, and the carbon dioxide feed inlet communicates with exhaust duct's exit end, being connected with carbon dioxide ejection of compact pipeline on the carbon dioxide discharge gate, being equipped with the carbon dioxide bleeder valve on the carbon dioxide ejection of compact pipeline, the exit end of carbon dioxide ejection of compact pipeline is connected with the storage jar.
Description
Technical field
This utility model belongs to round technical field, the spawn fermentation tank of a kind of band carbon dioxide treatment device being applied on the products such as fruit-vegetable food, medicine, health product.
Background technology
At present, the fermenting beverage product on market, various in style.Manufacturer both at home and abroad, mainly with Japan and TaiWan, China as representative, it mainly uses traditional dry method fermentation method or Unareobic fermentation to prepare, and is placed in by strain in the container such as cylinder of Plastic Drum or ceramic, is placed on vexed tank anaerobic fermentation in general Factory Building.In sweat, substantial amounts of carbon dioxide can be produced, in prior art, it is usually and the carbon dioxide of generation is directly discharged in air, not only can affect some environmental problems such as greenhouse effect, also not meeting present environmental protection concept and sustainable development policy, the product of strain fermentation is the health in order to assist human body, threatens healthy generation of human body the most on the contrary.
Utility model content
In order to overcome the deficiencies in the prior art, this utility model provides the fermentation tank of a kind of band carbon dioxide treatment device, the carbon dioxide produced in sweat is compressed into available product by pressurized carbon dioxide compression apparatus, the problem not only solving air pollution, the side-product of generation creates new economic benefit.
nullTo achieve these goals，The technical solution adopted in the utility model is: the fermentation tank of a kind of band carbon dioxide treatment device，Including tank body、Agitating device and music apparatus，Tank body top is provided with charge door，Tank body lower part is provided with discharging opening，Discharging opening connects discharge pipe，This discharge pipe is provided with outlet valve，It is characterized in that: described tank body top is provided with air vent，Connect on air vent and have discharge duct，This discharge duct is provided with air bleeding valve，The port of export of described discharge duct connects pressurized carbon dioxide compression apparatus，Pressurized carbon dioxide compression apparatus be respectively provided on two sides with feed carbon dioxide mouth and carbon dioxide discharging opening，Feed carbon dioxide mouth connects with the port of export of discharge duct，Connect on described carbon dioxide discharging opening and have carbon dioxide discharge pipe，Carbon dioxide discharge pipe is provided with carbon dioxide outlet valve，The port of export of carbon dioxide discharge pipe connects storage tank.
In said structure, the carbon dioxide produced in sweat is entered pressurized carbon dioxide compression apparatus by discharge duct, after the compressed liquefaction of carbon dioxide, discharge from carbon dioxide discharging opening and be stored in storage tank, side-product in storage tank can be by being further processed into the product of correspondence, during such as the product of fruit and vegerable one class of fermenting, can be with certain fragrance in the carbon dioxide produced, so carbon dioxide after compression can be made into the essence etc. of food processing, new economic benefit is created for fermentation procedure, reduce production cost, and accomplish carbon dioxide zero discharge, alleviation greenhouse effect and air pollution are contributed, environment friendly and pollution-free Zymolysis Equipment is provided, improve Zymolysis Equipment, adhere to sustainable development.
As further setting of the present utility model, it is provided with filter assemblies between described discharge duct and pressurized carbon dioxide compression apparatus, filter assemblies is provided with air inlet and gas outlet, the port of export of discharge duct connects with air inlet, connect on described gas outlet and have outlet pipe, outlet pipe is provided with air outlet valve, and the port of export of outlet pipe connects with the feed carbon dioxide mouth of pressurized carbon dioxide compression apparatus.
In said structure, the carbon dioxide produced in sweat may be mingled with some antibacterials or other impurity, and because fermentation temperature is higher, the impurity such as easy breed bacteria, through filter assemblies, other impurity such as the antibacterial in carbon dioxide are removed, obtain purer carbon dioxide, and different composition compression environment differences, such as environmental conditions such as compression temperatures, if impurities in carbon dioxide is too many, compression is not exclusively, cause compression efficiency relatively low, and compression after side-product of low quality, reproduction may be cannot be carried out utilize, though having processed carbon dioxide, but can not be directly proportional to the cost put into, economic benefit is the highest, if filtering accuracy is high, can be used directly after carbon dioxide compression liquefaction after filtering, without carrying out secondary operations, cost-effective.
As further setting of the present utility model, connect on described tank body and have logical oxygen channel, tank body offers tank body oxygen inlet, tank body oxygen inlet is connected with the logical oxygen channel port of export, logical oxygen channel arrival end is provided with steam inlet valve, exhaust-valve and intake valve, the logical oxygen channel port of export is provided with air inlet master control valve, tank body lower part is coated with insulation body, insulation body has the groove appeared so that local tank surface, music player one end is contacted with tank surface by this groove, this insulation body is hollow structure, insulation body is provided with steam (vapor) outlet and cooling water inlet, insulation body connects exogenous steam pipeline, exogenous steam pipeline is provided with steam valve and outlet valve, it is also associated with inlet channel on insulation body, this inlet channel is provided with water intaking valve.
In said structure, after tank body first passes around exhaust-valve aerofluxus, being passed through steam sterilization, especially the insulation body dual vapour source heat sterilization in tank and outside tank, can eliminate the miscellaneous bacteria at the various dead angle of tank body, it is ensured that sweat is in without miscellaneous bacteria state；Additionally, on this tank body and on insulation body, temperature probe all can be set and measure temperature in real time, ensure that probiotics is fermented at optimum temperature, above-mentioned insulation body is passed through while tank body is played sterilization functions by steam also to have and is incubated the effect to optimum fermentation temp, when temperature is too high, cold water can be passed through by inlet channel and lower the temperature and stabilize it in optimum temperature；Additionally, open music player during the fermentation, the probiotic bacteria being delivered in tank body to make in fermentation tank by the vibrations of music ripple can keep lasting excitatory state, accelerates its reproduction speed so that it is more vigourous.The filtrated air through sterilization treatment can be passed through by intake valve on above-mentioned logical oxygen channel, use airlift principle, improve mixing effect so that probiotics can be fermented in aerobic environment, it is to avoid probiotics long time sedimentation is in anaerobic state in tank base.
As further setting of the present utility model, being provided with strain observation window in the middle part of described tank body, tank body lower part is additionally provided with traversing carriage, and this traversing carriage includes the some columns being set up in tank body lower part, column upper end is around forming the mounting groove adaptive with tank body lower part, and column lower end is provided with roller.
In said structure, because the general volume of fermentation tank is relatively big, so being inconvenient to move, the Stability Analysis of Structures of traversing carriage and being be easily moved, facilitate using and cleaning of fermentation tank.
Use such scheme, by carbon dioxide after simple process, not only do not pollute the environment, and can also produce new economic benefit, simple in construction, but the effect reached is apparent from, and after the treated processing of carbon dioxide, the product of green non-pollution can be made, can be relieved as edible additives such as food interpolations, ensure the health of human body.
Below in conjunction with the accompanying drawings this utility model is further described.
Accompanying drawing explanation
Accompanying drawing 1 is this utility model specific embodiment schematic appearance；
Accompanying drawing 2 is the STRUCTURE DECOMPOSITION figure of this utility model specific embodiment tank body.
Detailed description of the invention
Below by embodiment, this utility model is specifically described; it is served only for this utility model is further described; it is not intended that the restriction to this utility model protection domain, this utility model can be made some nonessential improvement and adjustment according to the content of above-mentioned utility model by the technician in this field.
nullSpecific embodiment of the utility model is as shown in Figure 1-2，A kind of fermentation tank of band carbon dioxide treatment device，Including tank body 1、Agitating device 2 and music apparatus 3，Tank body top 11 is provided with charge door 111，Tank body lower part 13 is provided with discharging opening 131，Discharging opening 131 connects discharge pipe 132，This discharge pipe 132 is provided with outlet valve 133，Described tank body top 11 is provided with air vent 112，Connect on air vent 112 and have discharge duct 113，This discharge duct 113 is provided with air bleeding valve 114，The port of export of described discharge duct 113 connects pressurized carbon dioxide compression apparatus 4，Pressurized carbon dioxide compression apparatus 4 be respectively provided on two sides with feed carbon dioxide mouth 41 and carbon dioxide discharging opening 42，Feed carbon dioxide mouth 41 connects with the port of export of discharge duct 113，Connect on described carbon dioxide discharging opening 42 and have carbon dioxide discharge pipe 421，Carbon dioxide discharge pipe 421 is provided with carbon dioxide outlet valve 422，The port of export of carbon dioxide discharge pipe 421 connects storage tank 5.The carbon dioxide produced in sweat is entered pressurized carbon dioxide compression apparatus 4 by discharge duct 113, after the compressed liquefaction of carbon dioxide, discharge from carbon dioxide discharging opening 42 and be stored in storage tank 5, side-product in storage tank 5 can be by being further processed into the product of correspondence, during such as the product of fruit and vegerable one class of fermenting, can be with certain fragrance in the carbon dioxide produced, so carbon dioxide after compression can be made into the essence etc. of food processing, new economic benefit is created for fermentation procedure, reduce production cost, and accomplish carbon dioxide zero discharge, alleviation greenhouse effect and air pollution are contributed, environment friendly and pollution-free Zymolysis Equipment is provided, improve Zymolysis Equipment, adhere to sustainable development.
It is provided with filter assemblies 6 between above-mentioned discharge duct 113 and pressurized carbon dioxide compression apparatus 4, filter assemblies 6 is provided with air inlet 61 and gas outlet 62, the port of export of discharge duct 113 connects with air inlet 61, connect on described gas outlet 62 and have outlet pipe 621, outlet pipe 621 is provided with air outlet valve 622, and the port of export of outlet pipe 621 connects with the feed carbon dioxide mouth 41 of pressurized carbon dioxide compression apparatus 4.The carbon dioxide produced in sweat may be mingled with some antibacterials or other impurity, and because fermentation temperature is higher, the impurity such as easy breed bacteria, through filter assemblies 6, other impurity such as the antibacterial in carbon dioxide are removed, obtain purer carbon dioxide, and different composition compression environment differences, such as environmental conditions such as compression temperatures, if impurities in carbon dioxide is too many, compression is not exclusively, cause compression efficiency relatively low, and compression after side-product of low quality, reproduction may be cannot be carried out utilize, though having processed carbon dioxide, but can not be directly proportional to the cost put into, economic benefit is the highest, if filtering accuracy is high, can be used directly after carbon dioxide compression liquefaction after filtering, without carrying out secondary operations, cost-effective.
nullConnect on above-mentioned tank body 1 and have logical oxygen channel，Tank body 1 offers tank body oxygen inlet 71，Tank body oxygen inlet 71 is connected with the logical oxygen channel port of export，Logical oxygen channel arrival end is provided with steam inlet valve 72、Exhaust-valve 73 and intake valve 81，The logical oxygen channel port of export is provided with air inlet master control valve 82，Tank body lower part 13 is coated with insulation body 9，Insulation body 9 has so that the groove of local tank body 1 surface open，Music player 3 one end is contacted with tank body 1 surface by this groove，This insulation body 9 is hollow structure，Insulation body 9 is provided with steam (vapor) outlet 91 and cooling water inlet 92，Insulation body 9 connects exogenous steam pipeline，Exogenous steam pipeline is provided with steam valve 101 and outlet valve 102，It is also associated with inlet channel 93 on insulation body 9，This inlet channel 93 is provided with water intaking valve 94.After tank body 1 first passes around exhaust-valve 73 aerofluxus, being passed through steam sterilization, especially the muff 9 dual vapour source heat sterilization in tank and outside tank, can eliminate the miscellaneous bacteria at the various dead angle of tank body 1, it is ensured that sweat is in without miscellaneous bacteria state；Additionally, on this tank body 1 and on insulation body 9, temperature probe all can be set and measure temperature in real time, ensure that probiotics is fermented at optimum temperature, above-mentioned insulation body 7 is passed through while tank body 1 is played sterilization functions by steam also to have and is incubated the effect to optimum fermentation temp, when temperature is too high, cold water can be passed through by inlet channel 93 and lower the temperature and stabilize it in optimum temperature；Additionally, open music player 3 during the fermentation, the probiotic bacteria being delivered in tank body 1 to make in fermentation tank by the vibrations of music ripple can be kept lasting excitatory state, accelerate its reproduction speed so that it is more vigourous.The filtrated air through sterilization treatment can be passed through by intake valve 81 on above-mentioned logical oxygen channel, use airlift principle, improve mixing effect so that probiotics can be fermented in aerobic environment, it is to avoid probiotics long time sedimentation is in anaerobic state bottom tank body 1.
In the middle part of above-mentioned tank body, 12 are provided with strain observation window 121, tank body lower part 13 is additionally provided with traversing carriage 01, this traversing carriage 01 includes the some columns 011 being set up in tank body lower part 13, and column 011 upper end is around the mounting groove 012 formed with tank body lower part 13 adaptation, and column 011 lower end is provided with roller 013.Because the general volume of fermentation tank is relatively big, so being inconvenient to move, the Stability Analysis of Structures of traversing carriage 01 and being be easily moved, facilitate using and cleaning of fermentation tank.
Claims (4)
1. the fermentation tank of a band carbon dioxide treatment device, including tank body, agitating device and music apparatus, tank body top is provided with charge door, tank body lower part is provided with discharging opening, discharging opening connects discharge pipe, this discharge pipe is provided with outlet valve, it is characterized in that: described tank body top is provided with air vent, connect on air vent and have discharge duct, this discharge duct is provided with air bleeding valve, the port of export of described discharge duct connects pressurized carbon dioxide compression apparatus, pressurized carbon dioxide compression apparatus be respectively provided on two sides with feed carbon dioxide mouth and carbon dioxide discharging opening, feed carbon dioxide mouth connects with the port of export of discharge duct, connect on described carbon dioxide discharging opening and have carbon dioxide discharge pipe, carbon dioxide discharge pipe is provided with carbon dioxide outlet valve, the port of export of carbon dioxide discharge pipe connects storage tank.
The fermentation tank of a kind of band carbon dioxide treatment device the most according to claim 1, it is characterized in that: between described discharge duct and pressurized carbon dioxide compression apparatus, be provided with filter assemblies, filter assemblies is provided with air inlet and gas outlet, the port of export of discharge duct connects with air inlet, connect on described gas outlet and have outlet pipe, outlet pipe is provided with air outlet valve, and the port of export of outlet pipe connects with the feed carbon dioxide mouth of pressurized carbon dioxide compression apparatus.
The fermentation tank of a kind of band carbon dioxide treatment device the most according to claim 1, it is characterized in that: connecting on described tank body has logical oxygen channel, tank body offers tank body oxygen inlet, tank body oxygen inlet is connected with the logical oxygen channel port of export, logical oxygen channel arrival end is provided with steam inlet valve, exhaust-valve and intake valve, the logical oxygen channel port of export is provided with air inlet master control valve, tank body lower part is coated with insulation body, insulation body has the groove appeared so that local tank surface, music player one end is contacted with tank surface by this groove, this insulation body is hollow structure, insulation body is provided with steam (vapor) outlet and cooling water inlet, insulation body connects exogenous steam pipeline, exogenous steam pipeline is provided with steam valve and outlet valve, it is also associated with inlet channel on insulation body, this inlet channel is provided with water intaking valve.
The fermentation tank of a kind of band carbon dioxide treatment device the most according to claim 1, it is characterized in that: in the middle part of described tank body, be provided with strain observation window, tank body lower part is additionally provided with traversing carriage, this traversing carriage includes the some columns being set up in tank body lower part, column upper end is around forming the mounting groove adaptive with tank body lower part, and column lower end is provided with roller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620380694.0U CN205576116U (en) | 2016-04-28 | 2016-04-28 | Take carbon dioxide processing apparatus's fermentation cylinder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620380694.0U CN205576116U (en) | 2016-04-28 | 2016-04-28 | Take carbon dioxide processing apparatus's fermentation cylinder |
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| Publication Number | Publication Date |
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| CN205576116U true CN205576116U (en) | 2016-09-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620380694.0U Expired - Fee Related CN205576116U (en) | 2016-04-28 | 2016-04-28 | Take carbon dioxide processing apparatus's fermentation cylinder |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108342311A (en) * | 2018-04-20 | 2018-07-31 | 郑晓梅 | A kind of chemical reaction equipment |
| CN108359596A (en) * | 2018-04-20 | 2018-08-03 | 郑晓梅 | A kind of biochemistry equipment |
| CN108359595A (en) * | 2018-04-20 | 2018-08-03 | 郑晓梅 | A kind of biofermentation reaction unit |
-
2016
- 2016-04-28 CN CN201620380694.0U patent/CN205576116U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108342311A (en) * | 2018-04-20 | 2018-07-31 | 郑晓梅 | A kind of chemical reaction equipment |
| CN108359596A (en) * | 2018-04-20 | 2018-08-03 | 郑晓梅 | A kind of biochemistry equipment |
| CN108359595A (en) * | 2018-04-20 | 2018-08-03 | 郑晓梅 | A kind of biofermentation reaction unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160914 Termination date: 20190428 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |