CN215123987U - Production facility of high concentration coffee - Google Patents
Production facility of high concentration coffee Download PDFInfo
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- CN215123987U CN215123987U CN202121712232.1U CN202121712232U CN215123987U CN 215123987 U CN215123987 U CN 215123987U CN 202121712232 U CN202121712232 U CN 202121712232U CN 215123987 U CN215123987 U CN 215123987U
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Abstract
The utility model discloses a production facility of high concentration coffee, including soaking tank support, soaking tank is installed to soaking tank support's upper end, agitating unit is installed to soaking tank's inboard, soaking tank's top is provided with the conveyer belt of weighing, the top of conveyer belt of weighing is provided with grinds the machine. A production facility of high concentration coffee, the process flow has been simplified, the process cost is reduced, the loss of material in numerous and complicated process has been reduced, thereby can obtain the highest dissolution rate, can compromise and obtain high concentration coffee and need not the concentration again, the effective component dissolution rate is higher than 90%, high concentration coffee solution concentration (TDS concentration) is greater than 16%, coffee grounds moisture content is less than 10%, the yield exceeds 25%, be higher than current 10-15% yield far away, original component in the coffee has fully been kept, fragrance, especially abundant lipid material has been obtained, make coffee product taste mellow more.
Description
Technical Field
The utility model relates to a coffee production field, in particular to production facility of high concentration coffee.
Background
The production equipment of the high-concentration coffee solution is the production equipment for deep processing of coffee and is applied to the production occasions of the high-concentration coffee solution.
The existing high-concentration coffee liquid is prepared by concentrating low-concentration coffee liquid, the coffee concentrated liquid adopts a traditional brewing method to obtain low-concentration coffee liquid containing dregs, the low-concentration coffee liquid is obtained by filtering or centrifugal solid-liquid separation, and the lower-concentration coffee liquid is gradually concentrated into the higher-concentration coffee liquid by adopting technological methods such as evaporation, vacuum concentration or freeze concentration. The process for concentrating the low-concentration coffee solution into the high-concentration coffee solution is complex, the process consumption and the workload are large, the yield is low (the yield of soluble solid substances is about 10 to 12 percent), most of active ingredients such as lipid substances in the coffee cannot be separated out, and the separated parts are lost in the concentration process, so that the coffee brewed by the coffee concentrated solution or the instant coffee produced by the coffee concentrated solution almost completely loses the flavor and the taste of the coffee. In order to meet the market demand, manufacturers can only add flavoring agents or spices in the production process to prepare the taste which can be accepted by the market, so that the original flavor of the coffee is lost due to the loss of effective components of the coffee, and the products produced by the adding, preparing and other modes have low quality and are subject to wide scaling, so that the industry needs a convenient production device which can produce the high-concentration coffee without concentration.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a production facility of high concentration coffee can effectively solve the problem in the background art.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a production facility of high concentration coffee, includes soaking tank support, soaking tank is installed to soaking tank support's upper end, agitating unit is installed to soaking tank's inboard, soaking tank's top is provided with the conveyer belt of weighing, the top of conveyer belt of weighing is provided with grinds the machine, soaking tank's upper end is installed the pure water pipe, install first measuring pump before pure water pipe's the export, pipeline is installed to soaking tank's lower part export, pipeline's the outside is installed the second measuring pump, pipeline's one end is installed the frame, the extrusion chamber is installed to the upper end of frame, the upper end in extrusion chamber is installed out the cinder pan, the scraper blade pneumatic cylinder is installed to the top of going out the cinder pan, the scraper blade is installed to one side of scraper blade pneumatic cylinder, the gland pneumatic cylinder is installed to the inboard of scraper blade pneumatic cylinder, the gland is installed to the lower extreme of gland, the externally mounted of frame has the filtration cabin, the internally mounted of filtration cabin has the polymer filter core, the internally mounted of frame has piston pneumatic cylinder, the piston is installed to piston pneumatic cylinder's upper end, the catch tray is installed in the outside of frame, the drain pipe is installed to one side of catch tray, cold-stored storage tank is installed to the one end of drain pipe, the internally mounted of cold-stored storage tank has the output tube, the third metering pump is installed to the one end of output tube, the below of going out the slag pan is provided with band conveyer.
Preferably, one side of the gland hydraulic cylinder is provided with a gland lower dead point sensor and a gland upper dead point sensor, and the gland upper dead point sensor is positioned above the gland lower dead point sensor.
Preferably, one side of the extrusion cavity is provided with a piston vertex sensor, a piston top dead center sensor and a piston bottom dead center sensor, and the piston vertex sensor, the piston top dead center sensor and the piston bottom dead center sensor are sequentially arranged from top to bottom.
Preferably, a temperature sensor is installed in front of the refrigerating storage tank.
Preferably, a weighing sensor is arranged in the weighing conveyer belt.
Preferably, the inner sides of the gland and the extrusion cavity are both provided with gland seals, and the gland is positioned above the extrusion cavity.
Preferably, the lower end of the filtering cabin is provided with a base seal, and the filtering cabin is positioned below the extrusion cavity.
Preferably, the piston is movably connected with the base and the inner wall of the extrusion cavity, and the piston moves up and down along the inner axis by being positioned by the base.
Compared with the prior art, the utility model discloses following beneficial effect has:
1: the utility model discloses based on high concentration coffee can not solid-liquid separation through filtration or centrifugation and low concentration coffee must obtain the technology pain point of high concentration coffee through the concentration, the innovation has proposed the method that adopts high-pressure filter-pressing to obtain high concentration coffee, need not the concentration can produce high concentration coffee, simplified process flow, reduced process cost, reduced the loss of material in the numerous and complicated technological process;
2: the utility model develops research aiming at the problems that when water is added, part of coffee powder can not be soaked, when water is added, part of liquid can be leached, and the concentration of the coffee liquid is reduced, and the optimal powder-water ratio is 1:1.8 at normal temperature, so that the highest dissolution rate can be obtained, the highest yield can be obtained, and the high-concentration coffee liquid can be obtained without concentration;
3: the utility model adopts the method of extruding the water-containing coffee powder under high pressure with the pressure intensity of more than 5MPa, which not only forces the water in the coffee powder to wrap the soluble effective components and separate out together, but also extrudes the lipid substances insoluble in water, the dissolution rate of the effective components is higher than 90 percent, the concentration (TDS concentration) of the high-concentration coffee solution is more than 16 percent, the water content of the coffee grounds is less than 10 percent, the yield exceeds 25 percent and is far higher than the prior yield of 10 to 12 percent;
4: by adopting a pure physical extrusion method at normal temperature, most of effective components and lipid substances in the coffee are fully separated out, so that the content of the lipid substances in the high-concentration coffee liquid is higher than that of the coffee ground by hand, the original flavor of the raw material coffee is completely reserved, the original components and aroma of the coffee are fully reserved, particularly rich lipid substances are obtained, and the taste of the coffee product is mellow.
Drawings
FIG. 1 is a schematic view of the overall structure of a device for producing high-concentration coffee of the present invention;
FIG. 2 is a structural diagram of an infusion part of a high concentration coffee producing apparatus according to the present invention;
FIG. 3 is a structural view of an extruding part of the apparatus for producing high concentration coffee of the present invention;
FIG. 4 is a view showing the structure of the high-concentration coffee production apparatus after the pressing cover of the pressing part is pressed;
FIG. 5 is a schematic diagram of the apparatus for producing high concentration coffee according to the present invention after the piston of the extruding portion ascends;
FIG. 6 is a structural diagram of the high concentration coffee production apparatus after the pressing cover of the pressing part is reset;
FIG. 7 is a structural view of a refrigerating storage part of a high concentration coffee producing apparatus according to the present invention;
fig. 8 is a control diagram of the cpu of the high-concentration coffee producing apparatus of the present invention.
In the figure: 101. a grinder; 102. weighing the conveyer belt; 103. a soaking tank; 104. a stirring device; 105. a soaking tank bracket; 106. a first metering pump; 107. a pure water pipe; 201. a delivery conduit; 202. a second metering pump; 203. a scraper hydraulic cylinder; 204. a squeegee; 205. a gland hydraulic cylinder; 206. a gland; 207. sealing a gland; 208. a slag discharging disc; 209. an extrusion chamber; 210. a filtration compartment; 211. a polymer filter element; 212. the machine base is sealed; 213. a liquid collecting tray; 214. a piston hydraulic cylinder; 215. a piston; 216. a machine base; 217. a liquid outlet pipe; 401. a weighing sensor; 404. a gland top dead center sensor; 405. a gland bottom dead center sensor; 406. a piston apex sensor; 407. a piston top dead center sensor; 408. a piston bottom dead center sensor; 409. a temperature sensor; 301. a refrigerating storage tank; 302. an output pipe; 303. a third metering pump; 304. a belt conveyor.
Detailed Description
In order to make the technical means, creation features, achievement purposes and functions of the present invention easy to understand, the present invention is further described below with reference to the following embodiments.
Example 1:
as shown in figures 1-8, the invention relates to a production device of high-concentration coffee liquid, which comprises an immersion tank support 105, an immersion tank 103 is arranged at the upper end of the immersion tank support 105, a stirring device 104 is arranged at the inner side of the immersion tank 103, a weighing conveyer belt 102 is arranged above the immersion tank 103, a grinder 101 is arranged above the weighing conveyer belt 102, a pure water pipe 107 is arranged at the upper end of the immersion tank 103, a first metering pump 106 is arranged in front of the outlet of the pure water pipe 107, a conveying pipeline 201 is arranged at the lower outlet of the immersion tank 103, a second metering pump 202 is arranged at the outer side of the conveying pipeline 201, a base 216 is arranged at one end of the conveying pipeline 201, a squeezing cavity 209 is arranged at the upper end of the base 216, a slag discharging disc 208 is arranged at the upper end of the squeezing cavity 209, a scraper hydraulic cylinder 203 is arranged above the slag discharging disc 208, a scraper 204 is arranged at one side of the scraper hydraulic cylinder 203, a gland hydraulic cylinder 205 is arranged at the inner side of the scraper 203, a gland 206 is installed at the lower end of a gland hydraulic cylinder 205, a filtering cabin 210 is installed outside a base 216, a polymer filter element 211 is installed inside the filtering cabin 210, a piston hydraulic cylinder 214 is installed inside the base 216, a piston 215 is installed at the upper end of the piston hydraulic cylinder 214, a liquid collecting tray 213 is installed on the outer side of the base 216, a liquid outlet pipe 217 is installed on one side of the liquid collecting tray 213, a refrigerating storage tank 301 is installed at one end of the liquid outlet pipe 217, an output pipe 302 is installed inside the refrigerating storage tank 301, a third metering pump 303 is installed at one end of the output pipe 302, and a belt conveyor 304 is arranged below the slag discharging tray 208;
in this embodiment, a gland bottom dead center sensor 405 and a gland top dead center sensor 404 are disposed on one side of the gland hydraulic cylinder 205, and the gland top dead center sensor 404 is located above the gland bottom dead center sensor 405;
in this embodiment, a piston vertex sensor 406, a piston top dead center sensor 407 and a piston bottom dead center sensor 408 are disposed on one side of the extrusion cavity 209, and the piston vertex sensor 406, the piston top dead center sensor 407 and the piston bottom dead center sensor 408 are sequentially arranged from top to bottom;
in addition, a temperature sensor 409 is installed in front of the refrigerating storage tank 301;
in the present embodiment, a load cell 401 is installed inside the weighing conveyer belt 102;
in the embodiment, the gland 206 and the inner side of the extrusion cavity 209 are both provided with a gland seal 207, and the gland 206 is positioned above the extrusion cavity 209;
in this embodiment, the lower end of the filter chamber 210 is provided with a base seal 212, and the filter chamber 210 is located below the extrusion chamber 209;
in this embodiment, the piston 215 is movably connected with the base 216 and the inner wall of the pressing chamber 209, and the piston 215 is positioned by the base 216 to move up and down along the inner axis.
An apparatus for producing a highly concentrated coffee liquid, comprising, in use, the steps of:
step 1: adding 100kg of Yunnan small-particle moderately roasted coffee beans into a grinder 101, grinding the coffee beans into powder at normal temperature to obtain ground coffee powder with 18-mesh granularity, conveying the ground coffee powder by a weighing conveyer belt 102, metering and inputting the ground coffee powder into an immersion tank 103 by a weighing sensor 401, conveying pure water by a pure water pipe 107 and metering by a first metering pump 106 according to the ratio of the powder to water 1:1.8, adding 180kg of normal temperature pure water, fully mixing and stirring in an immersion tank 103 by using a stirring device 104, and immersing for 50 minutes to obtain 280kg of high-water-content coffee powder which is full of water and has no liquid overflow.
Step 2: after the central processor PLC stops the stirring device 104 according to the preset soaking time, the second metering pump 202 is started, so that the soaked coffee powder is quantitatively input into the extrusion cavity 209 through the conveying pipeline 201;
and step 3: after the extrusion cavity 209 is filled with a certain amount of water-containing coffee powder, the central processing unit PLC starts the gland hydraulic cylinder and positions the gland 206 to move to a bottom dead point through the gland bottom dead point sensor 405, the piston hydraulic cylinder 214 is started to push the piston 215 to move upwards to extrude the coffee powder in the extrusion cavity 209 at a pressure higher than 5MPa, so that soluble substances and lipid substances dissolved in water in the coffee powder are forced to be extruded to form high-concentration coffee liquid, the high-concentration coffee liquid is separated from most coffee solid substances, 173.72kg and 106.28kg of coffee grounds can be separated, the central processing unit PLC controls the piston 215 to move to the top dead point through the piston top dead point sensor 407 to stop, and at the moment, the high-water-containing coffee powder in the extrusion cavity 209 is extruded into coffee dry powder with the water content lower than 10% and the effective soluble substance content lower than 3%;
and 4, step 4: the central processor PLC opens the piston hydraulic cylinder 214, pushes the piston 215 to the top dead center and stops, and high-concentration coffee liquid entering the filtering cabin 210 through the liquid outlet groove in the cavity is filtered by the polymer filter element 211 and then is extruded out of the liquid outlet groove outside the base 216, so that macromolecular suspended substances, pesticides and heavy metal residues in the liquid are removed; 163kg of a high-strength coffee liquor of higher clarity without any suspended and precipitated material were obtained;
and 5: after being collected by the liquid collecting disc 213, the extruded high-concentration coffee liquid is input into the refrigeration storage tank 301 from the high-concentration liquid outlet pipe 217 for storage, the refrigeration storage tank 301 has a freezing function, the high-concentration coffee liquid is stored at low temperature, cannot deteriorate within the quality guarantee period, and can be used for being filled into finished products or used for producing instant dry powder by a drying process;
step 6: and the piston hydraulic cylinder 214 is started again to move upwards to the top point, the upper plane of the piston 215 is flush with the slag discharging disc 208 at the moment, the central processor PLC starts the scraper hydraulic cylinder 203, the scraper 204 is pushed forwards to push the waste slag, the scraper 204 returns to the initial position, and the waste slag slides along the slope of the slag discharging disc 208 to the belt conveyor 304 to be discharged.
By the method, 163kg of finished high-concentration coffee liquor with high clarity and without any suspended and precipitated substances can be obtained by processing 100kg of Yunnan small-grain moderately roasted coffee beans, the TDS concentration is 16.38 percent (the content of soluble substances is 16.38 percent), and the yield of the soluble effective substances is 26.70 percent; 117kg of coffee grounds are separated, the content of the effective substances of the soluble coffee in the coffee grounds is 2.76%, and the extraction rate of the effective substances is 90.80%.
Example 2:
on the basis of example 1, a production apparatus for high-strength coffee comprises the following steps:
step 1: 100kg of blended deeply roasted coffee beans formed by blending 40% of columbia deeply roasted coffee beans, 20% of Eleobia deeply roasted coffee beans and 40% of Yunnan small-particle deeply roasted coffee beans are added into a grinder 101, the coffee beans are ground into powder at normal temperature to obtain ground coffee powder with 18 meshes, the ground coffee powder is conveyed by a weighing conveyer belt 102, a weighing sensor 401 is metered and input into an immersion tank 103, and pure water is conveyed through a pure water pipe 107 and a first metering pump 106 according to the ratio of 1:1.8, adding 180kg of normal temperature pure water, fully mixing and stirring in an immersion tank 103 by using a stirring device 104, and immersing for 50 minutes to obtain 280kg of high-water-content coffee powder which is full of water and has no liquid overflow.
Step 2: after the central processor PLC stops the stirring device 104 according to the preset soaking time, the second metering pump 202 is started, so that the soaked coffee powder is quantitatively input into the extrusion cavity 209 through the conveying pipeline 201;
and step 3: after the extrusion cavity 209 is filled with a certain amount of water-containing coffee powder, the central processing unit PLC starts the gland hydraulic cylinder and positions the gland 206 to move to a bottom dead point through the gland bottom dead point sensor 405, the piston hydraulic cylinder 214 is started to push the piston 215 to move upwards to extrude the coffee powder in the extrusion cavity 209 at a pressure higher than 5MPa, so that soluble substances and lipid substances dissolved in water in the coffee powder are forced to be extruded to form high-concentration coffee liquid and separated from most coffee solid substances, 171.66kg of high-concentration coffee solution and 108.34kg of coffee grounds are separated, the central processing unit PLC controls the piston 215 to move to the top dead point through the piston top dead point sensor 407 to stop, and at the moment, the high-water-containing coffee powder in the extrusion cavity 209 is extruded into coffee dry powder with the water content lower than 10% and the effective soluble substance content lower than 3%;
and 4, step 4: the central processor PLC opens the piston hydraulic cylinder 214, pushes the piston 215 to the top dead center and stops, and high-concentration coffee liquid entering the filtering cabin 210 through the liquid outlet groove in the cavity is filtered by the polymer filter element 211 and then is extruded out of the liquid outlet groove outside the base 216, so that macromolecular suspended substances, pesticides and heavy metal residues in the liquid are removed;
and 5: after being collected by the liquid collecting disc 213, the extruded high-concentration coffee liquid is input into the refrigeration storage tank 301 from the high-concentration liquid outlet pipe 217 for storage, the refrigeration storage tank 301 has a freezing function, the high-concentration coffee liquid is stored at low temperature, cannot deteriorate within the quality guarantee period, and can be used for being filled into finished products or used for producing instant dry powder by a drying process;
step 6: and the piston hydraulic cylinder 214 is started again to move upwards to the top, at the moment, the upper plane of the piston 215 is flush with the slag discharging disc 208, the central processing unit PLC starts the scraper hydraulic cylinder 203, pushes the scraper 204 to push the waste slag forwards, the scraper 204 returns to the initial position, the waste slag slides along the slope of the slag discharging disc 208 to the belt conveyor 304 to be discharged, and 161.72kg of high-clarity high-concentration coffee liquid without any suspended and deposited substances is obtained.
By the method, 161.72kg of high-concentration coffee liquor with high clarity and without any suspended and precipitated substances can be obtained by processing 100kg of blended deep-roasted coffee beans, the TDS concentration is 16.22 (the content of soluble substances is 16.22 percent), and the yield of the soluble effective substances is 26.23 percent; 118.28kg of coffee grounds are separated, the content of the effective substances of the soluble coffee in the coffee grounds is 2.66%, and the extraction rate of the effective substances is 91.13%.
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 production facility of high concentration coffee is characterized in that: including soaking tank support (105), soaking tank (103) is installed to the upper end of soaking tank support (105), agitating unit (104) are installed to the inboard of soaking tank (103), the top of soaking tank (103) is provided with weighing conveyer belt (102), the top of weighing conveyer belt (102) is provided with grinds machine (101), pure water pipe (107) is installed to the upper end of soaking tank (103), install first measuring pump (106) before the export of pure water pipe (107), pipeline (201) is installed to the lower part export of soaking tank (103), second measuring pump (202) is installed in the outside of pipeline (201), frame (216) is installed to the one end of pipeline (201), extrusion chamber (209) is installed to the upper end of frame (216), slag discharging dish (208) is installed to the upper end of extrusion chamber (209), the top of going out slag pan (208) installs scraper blade pneumatic cylinder (203), scraper blade (204) are installed to one side of scraper blade pneumatic cylinder (203), gland pneumatic cylinder (205) are installed to the inboard of scraper blade pneumatic cylinder (203), gland (206) are installed to the lower extreme of gland pneumatic cylinder (205), the externally mounted of frame (216) has filter chamber (210), the internally mounted of filter chamber (210) has polymer filter core (211), the internally mounted of frame (216) has piston pneumatic cylinder (214), piston (215) are installed to the upper end of piston pneumatic cylinder (214), liquid collecting pan (213) is installed in the outside of frame (216), drain pipe (217) are installed to one side of liquid collecting pan (213), cold-stored storage tank (301) is installed to the one end of drain pipe (217), the internally mounted of cold-stored storage tank (301) has output tube (302), and a third metering pump (303) is installed at one end of the output pipe (302), and a belt conveyor (304) is arranged below the slag discharging disc (208).
2. A high-strength coffee producing apparatus according to claim 1, wherein: one side of the gland hydraulic cylinder (205) is provided with a gland bottom dead center sensor (405) and a gland top dead center sensor (404), and the gland top dead center sensor (404) is located above the gland bottom dead center sensor (405).
3. A high-strength coffee producing apparatus according to claim 1, wherein: and a piston top sensor (406), a piston top dead center sensor (407) and a piston bottom dead center sensor (408) are arranged on one side of the extrusion cavity (209), and the piston top sensor (406), the piston top dead center sensor (407) and the piston bottom dead center sensor (408) are sequentially arranged from top to bottom.
4. A high-strength coffee producing apparatus according to claim 1, wherein: and a temperature sensor (409) is arranged in front of the refrigerating storage tank (301).
5. A production apparatus of a high concentration coffee liquid according to claim 4, characterized in that: and a weighing sensor (401) is arranged in the weighing conveyer belt (102).
6. A high-strength coffee producing apparatus according to claim 1, wherein: gland seals (207) are installed to the inboard of gland (206) and extrusion chamber (209), and gland (206) are located the top position in extrusion chamber (209).
7. A high-strength coffee producing apparatus according to claim 1, wherein: the lower end of the filtering cabin (210) is provided with a base seal (212), and the filtering cabin (210) is positioned below the extrusion cavity (209).
8. A high-strength coffee producing apparatus according to claim 1, wherein: the piston (215) is movably connected with the base (216) and the inner wall of the extrusion cavity (209), and the piston (215) is positioned by the base (216) to move up and down along the inner axis.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202121712232.1U CN215123987U (en) | 2021-07-27 | 2021-07-27 | Production facility of high concentration coffee |
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| CN202121712232.1U CN215123987U (en) | 2021-07-27 | 2021-07-27 | Production facility of high concentration coffee |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115769848A (en) * | 2022-12-09 | 2023-03-10 | 苏州金猫咖啡有限公司 | Instant coffee and production method and production device thereof |
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2021
- 2021-07-27 CN CN202121712232.1U patent/CN215123987U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115769848A (en) * | 2022-12-09 | 2023-03-10 | 苏州金猫咖啡有限公司 | Instant coffee and production method and production device thereof |
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