CN203960171U - Hops isomerization adding set - Google Patents
Hops isomerization adding set Download PDFInfo
- Publication number
- CN203960171U CN203960171U CN201420374797.7U CN201420374797U CN203960171U CN 203960171 U CN203960171 U CN 203960171U CN 201420374797 U CN201420374797 U CN 201420374797U CN 203960171 U CN203960171 U CN 203960171U
- Authority
- CN
- China
- Prior art keywords
- extraction tank
- hop extraction
- hops
- adding set
- hot water
- 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.)
- Expired - Fee Related
Links
Landscapes
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The related a kind of hops isomerization adding set of the utility model, on the basis of wheat juice hops adding set, increase pipeline, valve, impeller pump, heating and thermal insulation etc., have effective constituent alpha-acid in cycling extraction hops of one's own, carry out isomerization processing, thereby improve the utilization ratio of hops effective constituent, improve the quality that hops use simultaneously.
Description
Technical field
The utility model relates in a kind of beer production wort copper provided and adds hops device, and more particularly, it relates to a kind of hops isomerization adding set.
Background technology
At present, on market, add for beer production boiling pot the annex such as pump and pipeline valve that is equipped with that the device of hops is made up of two or more tanks and add hops in boiling pot, lack and the alpha-acid in hops is occurred under heated condition to for isomerization form iso-α-acid.
Utility model content
The deficiency existing for prior art, the purpose of this utility model is to provide a kind of hops isomerization adding set, has the advantages that the alpha-acid in hops is occurred under heated condition to for isomerization formation iso-α-acid.
For achieving the above object, the utility model provides following technical scheme:
A kind of hops isomerization adding set, comprise hop extraction tank, the top of described hop extraction tank is provided with CIP entrance, charging opening and overflow port, the middle part outer wall of described hop extraction tank is provided with hot water inlet, wheat juice entrance and Matter Transfer pipe, the bottom of described hop extraction tank is provided with Matter Transfer mouth and sewage draining exit, on described Matter Transfer pipe, stopping valve is installed, the outer wall of described hop extraction tank is connected with steam heating jacket.
The top of described hop extraction tank is that butterfly rotary pressed head is shaped, and its underpart is tapered bottom, angle <135 °, and described steam heating jacket is arranged on bottom and the bottom of hop extraction tank.
Hop extraction tank is provided with low liquid level demonstration and temperature shows control.
Described hop extraction tank and Matter Transfer pipe all adopt the insulation of silicate heat.
Described Matter Transfer pipe comprises CIP pipeline, brewing water pipeline, 90 DEG C of hot water pipelines, hot wheat juice pipeline and material outlet pipelines, on described 90 DEG C of hot water pipelines, be connected with the hot water impeller pump for hot water being sent into hop extraction tank, on described material outlet pipeline, be connected with the material impeller pump for the material of hop extraction tank is extracted out.
By adopting technique scheme, have effective constituent alpha-acid in cycling extraction hops of one's own, carry out isomerization processing, thereby improve the utilization ratio of hops effective constituent, improve the quality that hops use simultaneously.
Brief description of the drawings
Fig. 1 is the schematic diagram of the utility model hops isomerization adding set embodiment.
1, hop extraction tank; 2, heating jacket.
Embodiment
With reference to Fig. 1, the utility model hops isomerization adding set embodiment is described further.
A kind of hops isomerization adding set, comprise hop extraction tank 1, the top of described hop extraction tank 1 is provided with CIP entrance, charging opening and overflow port, the middle part outer wall of described hop extraction tank 1 is provided with hot water inlet, wheat juice entrance and Matter Transfer pipe, the bottom of described hop extraction tank 1 is provided with Matter Transfer mouth and sewage draining exit, on described Matter Transfer pipe, stopping valve is installed, the outer wall of described hop extraction tank 1 is connected with steam heating jacket 2.
The top of described hop extraction tank 1 is that butterfly rotary pressed head is shaped, and its underpart is tapered bottom, angle <135 °, and described steam heating jacket 2 is arranged on bottom and the bottom of hop extraction tank 1.
Hop extraction tank 1 is provided with low liquid level demonstration and temperature shows control.
Described hop extraction tank 1 all adopts the insulation of silicate heat with Matter Transfer pipe.
Described Matter Transfer pipe comprises CIP pipeline, brewing water pipeline, 90 DEG C of hot water pipelines, hot wheat juice pipeline and material outlet pipelines, on described 90 DEG C of hot water pipelines, be connected with the hot water impeller pump for hot water being sent into hop extraction tank 1, on described material outlet pipeline, be connected with the material impeller pump for the material of hop extraction tank 1 is extracted out.
Hop extraction tank 1 is to utilize alpha-acid being heated to 75～90 DEG C, pH value 6.5～7.5, and add quantitative oxydase and catalyzer, and to obtain the alpha-acid isomerization amount of a large amount, improve isomerization rate and can reach 30～50%, can save the total consumption 15～20% of hops.
Process implementing step:
1, hot water preparing in advance, plate changes steam heating or the heating of the bottom of a pan jacket steam, 75～90 DEG C of water temperatures, pump circulation primary makes even water temperature for approximately 3 minutes;
2, from the quantitative pellet hop of charging opening 12, add oxydase, catalyzer, adjust pH value, open recycle valve, pump carries out constant temperature circulating 5 minutes, is incubated 20～30 minutes, has both completed the isomerization process of alpha-acid, and isomerization rate reaches 30～50%;
3, the temperature of hop extraction tank 1 shows control;
This equipment also can doublely do syrup quantitatively to be added, and other hop product and additive are (as lactic acid, carrageenin, CaSO
4, Zn SO
4) interpolation use.
The above is only preferred implementation of the present utility model, and protection domain of the present utility model is also not only confined to above-described embodiment, and all technical schemes belonging under the utility model thinking all belong to protection domain of the present utility model.It should be pointed out that for those skilled in the art, in the some improvements and modifications that do not depart under the utility model principle prerequisite, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (5)
1. a hops isomerization adding set, it is characterized in that: comprise hop extraction tank, the top of described hop extraction tank is provided with CIP entrance, charging opening and overflow port, the middle part outer wall of described hop extraction tank is provided with hot water inlet, wheat juice entrance and Matter Transfer pipe, the bottom of described hop extraction tank is provided with Matter Transfer mouth and sewage draining exit, on described Matter Transfer pipe, stopping valve is installed, the outer wall of described hop extraction tank is connected with steam heating jacket.
2. hops isomerization adding set according to claim 1, it is characterized in that: the top of described hop extraction tank is that butterfly rotary pressed head is shaped, its underpart is tapered bottom, angle <135 °, and described steam heating jacket is arranged on bottom and the bottom of hop extraction tank.
3. hops isomerization adding set according to claim 1 and 2, is characterized in that: hop extraction tank is provided with low liquid level demonstration and temperature shows control.
4. hops isomerization adding set according to claim 3, is characterized in that: described hop extraction tank and Matter Transfer pipe all adopt the insulation of silicate heat.
5. hops isomerization adding set according to claim 4, it is characterized in that: described Matter Transfer pipe comprises CIP pipeline, brewing water pipeline, 90 DEG C of hot water pipelines, hot wheat juice pipeline and material outlet pipelines, on described 90 DEG C of hot water pipelines, be connected with the hot water impeller pump for hot water being sent into hop extraction tank, on described material outlet pipeline, be connected with the material impeller pump for the material of hop extraction tank is extracted out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420374797.7U CN203960171U (en) | 2014-07-05 | 2014-07-05 | Hops isomerization adding set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420374797.7U CN203960171U (en) | 2014-07-05 | 2014-07-05 | Hops isomerization adding set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203960171U true CN203960171U (en) | 2014-11-26 |
Family
ID=51920780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420374797.7U Expired - Fee Related CN203960171U (en) | 2014-07-05 | 2014-07-05 | Hops isomerization adding set |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203960171U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3269796A4 (en) * | 2015-03-10 | 2018-09-12 | Asahi Breweries, Ltd. | Method and device for manufacturing beer or beer-like beverage, and beer and beer-like beverage |
-
2014
- 2014-07-05 CN CN201420374797.7U patent/CN203960171U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3269796A4 (en) * | 2015-03-10 | 2018-09-12 | Asahi Breweries, Ltd. | Method and device for manufacturing beer or beer-like beverage, and beer and beer-like beverage |
| US10415006B2 (en) | 2015-03-10 | 2019-09-17 | Asahi Breweries, Ltd. | Method and apparatus for producing beer or beer-like beverage, and beer and beer-like beverage |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202626355U (en) | Solar cocoon cooking barrel | |
| CN202697632U (en) | Marinating tank | |
| CN105056871A (en) | Production device for thermal reaction essence | |
| CN203704320U (en) | Instant water boiler | |
| CN203960171U (en) | Hops isomerization adding set | |
| CN204224603U (en) | A kind of holothurian oral liquid production enzymolysis device | |
| CN203990561U (en) | Improve the reactor heater of conversion rate of products | |
| CN203692497U (en) | Fermentation tank capable of controlling temperature in real time | |
| CN201680567U (en) | Thermostatic medium hot water system for lysozyme fermentation liquid dispensing cylinder | |
| CN204816541U (en) | Apparatus for producing of thermal response essence | |
| CN101372653B (en) | Beer saccharification filter device using coil pipe for heating | |
| CN203857828U (en) | Exhaust heat recovery system of vanadium-nitrogen alloy production kiln | |
| CN204187599U (en) | A kind of still kettle afterheat steam recycling device | |
| CN103937672A (en) | Bioreactor thermostat | |
| CN204105768U (en) | Coffee maker box structure | |
| CN204429279U (en) | A kind of reactor conduction oil induction system | |
| CN210930876U (en) | Noodle boiling and noodle discharging equipment | |
| CN202830002U (en) | Energy-saving beer saccharification pot | |
| CN202022877U (en) | Simple wall sticking prevention amylodextrin circular heating device | |
| CN203764242U (en) | Double jacketed reaction kettle | |
| CN205137925U (en) | Prevent dry combustion method water heater inner bag | |
| CN202562320U (en) | Soda water mixing device | |
| CN202921299U (en) | Internal heating reaction kettle | |
| CN103743131B (en) | Improve method and the application system of the solar water heating system thermal efficiency and heat utilization efficiency | |
| CN106580067A (en) | Food cooking temperature regulation device |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141126 Termination date: 20200705 |