CN212911502U - Six clear tea goods production systems - Google Patents
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- CN212911502U CN212911502U CN202020495933.3U CN202020495933U CN212911502U CN 212911502 U CN212911502 U CN 212911502U CN 202020495933 U CN202020495933 U CN 202020495933U CN 212911502 U CN212911502 U CN 212911502U
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Abstract
The utility model discloses a six-root tea product production system, wherein the six-root tea product is prepared by using burdock root, lettuce root, reed root, dandelion root, kudzu-vine root, ginseng, dyers woad leaf, purslane, glabrous greenbrier rhizome and blackberry lily as main raw materials through the steps of water decoction, filtration, purification, spray drying and tabletting; the product is divided into acid tablet and alkali tablet. A six-root tea product production system comprises: the system comprises an acidic tablet raw material granulating system, an alkaline tablet raw material granulating system, an air inlet system, an air exhaust system and a raw material storing and distributing system; the system is characterized in that a plurality of devices are connected in series to form a production line, and the operation is stable.
Description
Technical Field
The utility model belongs to the food field, concretely relates to six clear tea goods production systems.
Background
The burdock has the effects of reducing blood pressure, strengthening spleen and stomach, tonifying kidney and strengthening yang, and has better tonifying effect on people with kidney deficiency and weakness; he can remove metabolic waste such as uric acid in vivo, and has effects of preventing and resisting cancer, promoting health and caring skin; it also has certain effect on modern diseases such as hyperlipemia, diabetes, rheumatoid disease and obesity.
In addition, the burdock also contains a very special substance which can help hormone secretion, thereby having the effects of strengthening essence, enhancing physical strength, helping brain development and discharging old wastes in vivo out of body. The burdock fiber contains a special enzyme which can help the beneficial bacteria growth in the intestine. People with constipation can eat more burdock, which can produce unexpected effect.
However, the burdock tea directly taken has bitter and pungent taste like grass roots, and many people who drink the burdock tea for the first time cannot accept the tea taste, but the tea is often seasoned by adding honey, red dates or crystal sugar. How to remove the bitter and pungent taste of the burdock and make the burdock become a favorite product is a problem worthy of discussion. In spite of the burdock products on the market at present, most of the burdock products are directly processed to prepare products, and few products are prepared by changing the flavor of the burdock products. Therefore, it would be a new attempt to add additional flavors and make an effervescent tablet form of burdock product by modifying the flavor of burdock.
Disclosure of Invention
To the technical problem who exists above, the utility model provides a six clear tea goods production systems, include: the device comprises an acidic tablet raw material granulating system, a basic tablet raw material granulating system, an air inlet system, an air exhaust system and a raw material storing and distributing system.
The acidic tablet raw material granulating system comprises a first air flow distribution plate and a shell of the acidic tablet raw material granulating system, wherein the lower part of the first air flow distribution plate is connected with a first air duct, the first air flow distribution plate is connected with the lower part of the shell of the acidic tablet raw material granulating system, a first fluidized granulating chamber, a first spray drying chamber and a first filtering chamber are sequentially arranged in the shell of the acidic tablet raw material granulating system from bottom to top, a first catching bag and a second catching bag are arranged at the upper part of the first filtering chamber, a first air cylinder is connected outside the first catching bag and the second catching bag, and the lower part of the first filtering chamber is connected to the raw material storing and; the top of the first filtering chamber is connected with the exhaust system through a pipeline;
the alkaline tablet raw material granulating system comprises an air flow distribution plate II and an alkaline tablet raw material granulating system shell, wherein the lower part of the air flow distribution plate II is connected with an air duct II, the air flow distribution plate II is connected with the lower part of the alkaline tablet raw material granulating system shell, a fluidized granulating chamber II, a spray drying chamber II and a filter chamber II are sequentially arranged in the alkaline tablet raw material granulating system shell from bottom to top, a trapping bag III and a trapping bag IV are arranged at the upper part of the filter chamber II, an air cylinder II is externally connected with the trapping bag III and the trapping bag IV, and the lower part of the filter chamber II is connected to a raw material storing and distributing system through a nozzle; the top of the second filtering chamber is connected with the exhaust system through a pipeline;
the air inlet system comprises an air filter and a heater connected with the air filter, and the heater is connected to the first air channel through a first air door and is connected to the second air channel through a second air door;
the air exhaust system comprises an induced draft fan, an air exhaust valve I and an air exhaust valve II, the induced draft fan is connected with the first filter chamber through the first air exhaust valve, and the induced draft fan is connected with the second filter chamber through the second air exhaust valve;
the raw material storage and distribution system comprises a first raw material tank, a second raw material tank, a third raw material tank and a fourth raw material tank, wherein the first raw material tank, the second raw material tank and the third raw material tank are connected to a first nozzle through a first pipeline liquid mixer, and a first metering pump, a second metering pump and a third metering pump are sequentially arranged among the first raw material tank, the second raw material tank, the third raw material tank and the first liquid mixer; the raw material tank II, the raw material tank III and the raw material tank four-way are connected to the nozzle II through the liquid mixer II; and a metering pump IV, a metering pump V and a metering pump VI are sequentially arranged among the stock tank II, the stock tank III, the stock tank IV and the liquid mixer II.
Furthermore, the first air door and the first air door are periodically opened and closed, when the first air door is opened, the second air door is closed, the second air cylinder pumps compressed air to the third trapping bag and the fourth trapping bag in the second filtering chamber through the pipelines, particles attached to the third trapping bag and the fourth trapping bag in the second filtering chamber are shaken into the second fluidized granulation chamber and can be periodically taken out from the second discharging port, otherwise, the second air door is opened, the first air door is closed, the first air cylinder pumps compressed air to the third trapping bag and the fourth trapping bag in the first filtering chamber through the pipelines, the particles attached to the first trapping bag in the first filtering chamber and the second trapping bag are shaken into the first fluidized granulation chamber and can be periodically taken out from the first discharging port. The acid tablet component and the alkali tablet component are separately collected, so that the consumption caused by acid-base neutralization reaction between organic acid in the acid tablet and inorganic base in the alkali tablet can be avoided.
Furthermore, the first liquid mixer and the second liquid mixer are the same in specification and respectively comprise an annular liquid mixing area, an inner annular wall of the annular liquid mixing area, a first shower nozzle, a second solution inlet pipeline and a third solution inlet pipeline, one end of the annular liquid mixing area is provided with a liquid inlet bell mouth, and the opposite end of the liquid inlet bell mouth is provided with a liquid outlet bell mouth; the second solution liquid inlet pipeline penetrates through the inner annular wall of the annular liquid mixing zone, the first shower nozzle is arranged at one end, opposite to the first liquid inlet bell mouth, of the second solution liquid inlet pipeline, and the first solution liquid inlet pipeline is connected to the first liquid inlet bell mouth; three inlet line of solution run through the interior rampart in annular liquid mixing district, shower nozzle two sets up the one end of going out liquid horn mouth relatively at three inlet line of solution, it leads to the liquid outlet to go out liquid horn mouth, and the raw materials in raw material tank one, raw material tank two, the raw material tank three are solution one, solution two, solution three of liquid mixer one respectively, and is the same, and to liquid mixer two, the raw materials in raw material tank two, raw material tank three, the raw material tank four are solution one, solution two, solution three respectively, and solution one mixes with solution three after the inlet horn mouth mixes again.
Furthermore, the first shower head and the second shower head are both spherical shower heads and are provided with a plurality of liquid outlet through holes.
Furthermore, the flow rates of the first metering pump, the second metering pump, the third metering pump, the fourth metering pump, the fifth metering pump and the sixth metering pump are adjustable, namely the mixing proportion of the liquid introduced into the first liquid mixer and the second liquid mixer is adjustable, so that the mixing proportion of the liquid can be adjusted by changing the flow rate of the metering pumps to meet the production requirement when the process is modified.
The working principle of the production system of the six-root tea product is as follows: liquid in the first raw material tank, the second raw material tank and the third raw material tank obtained in the sixth step is sent to the first liquid mixer in proportion through the first metering pump, the second metering pump and the third metering pump to be mixed, then is pressurized by compressed air in the first air pipeline and the second air pipeline, and then is sent to the first nozzle, and liquid in the second raw material tank, the third raw material tank and the fourth raw material tank obtained in the sixth step is sent to the second liquid mixer in proportion through the fourth metering pump, the fifth metering pump and the sixth metering pump to be mixed, then is pressurized by compressed air in the third air pipeline and the fourth air pipeline, and then is sent to the second nozzle;
air is heated by a heater after passing through an air filter under the suction of negative pressure, is sent to the first air supply channel through the first air door and is sent to the first air supply channel through the second air door, enters the first fluidized granulation chamber from the first air flow distribution plate, and is stirred and suspended into fluidization and mixed; the seed powder enters a second fluidization granulation chamber from the second air flow distribution plate, and is stirred and suspended into fluidization and mixed;
liquid materials are conveyed to the first nozzle from the first raw material tank, the second raw material tank and the third raw material tank, are conveyed to the second nozzle from the second raw material tank, the third raw material tank and the fourth raw material tank, are atomized into fine liquid drops by compressed air, one part of the fine liquid drops is used as a wetting adhesive to be sprayed on fluidized powder in the first fluidized bed granulation chamber and the second fluidized bed granulation chamber to be cemented into a mass for granulation, and the other part of air is dried by rising hot air flow and is brought to the first filter chamber and the second filter chamber;
the temperature of the airflow passing through the first fluidized bed granulation chamber and the second fluidized bed granulation chamber is sharply reduced, at the moment, the auxiliary fan blows hot airflow around the nozzle through the blast pipe, and the hot airflow rises along the spray drying chamber under the suction force of the induced draft fan, so that the temperatures of the spray drying chamber and the filter chamber are improved, and fine liquid drops brought to the first filter chamber and the second filter chamber along with the airflow are fully dried;
the dry powder is collected by a first collecting bag and a second collecting bag, after a certain amount of powder is obtained, a first air door is closed, a second air door is opened, meanwhile, a first air cylinder pumps compressed air to the first collecting bag and the second collecting bag in a first filtering chamber through pipelines, particles attached to the first collecting bag and the second collecting bag in the first filtering chamber are shaken into a first fluidized granulating chamber, and the particles can be periodically taken out from a first discharging port; and on the contrary, when the air door I is opened, the air door II is closed, the air cylinder II pumps compressed air to the trapping bag III and the trapping bag IV in the filtering chamber II through the pipeline, particles attached to the trapping bag III and the trapping bag IV in the filtering chamber II are shaken into the fluidized granulating chamber II and can be taken out from the discharge port II periodically, and therefore the whole spray drying granulating operation is completed.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model provides a six-root tea-leaves which is prepared by taking burdock root, lettuce root, reed root, dandelion root, kudzu root and ginseng as main materials, inorganic alkali, organic acid, filling agent, color correcting agent and flavoring agent as auxiliary materials, wherein the main materials are extracted by water decoction twice, and the ethanol purification process has higher utilization rate of beneficial components compared with direct water soaking or physical crushing, and has less harmful components, two tablets are arranged in a packaging bag after the tablets are prepared, the six-root tea-leaves have the flavor of citrus fruit, the alkali tablet has the flavor of liquorice, the acid tablet and the alkali tablet are put into water simultaneously, and the effervescent effect of the effervescent tablet can be generated, the six-root tea-leaves contain various flavors, and have the components of nourishing and health preserving of traditional Chinese medicine, and also have the bubble effect of the effervescent tablet, wherein, the main materials of burdock root, lettuce root, reed root, dandelion root, kudzu root and ginseng all have the effects of clearing heat and removing fire, in a word, the invention has various tastes, and has the effects of nourishing, preserving health, clearing heat and removing fire and good health care effect.
Drawings
Fig. 1 is a schematic diagram of the overall structure of a six-root tea product production system.
Fig. 2 is a schematic view of the overall structure of the liquid mixer.
Wherein, 1-an air filter, 2-a heater, 3 a-an air door I, 3 b-an air door II, 4 a-an air duct I, 4 b-an air duct II, 5 a-an air flow distribution plate I, 5 b-an air flow distribution plate II, 6 a-a fluidization granulation chamber I, 6 b-a fluidization granulation chamber II, 7 a-a discharge port I, 7 b-a discharge port II, 8 a-a nozzle I, 8 b-a nozzle II, 9 a-a spray drying chamber I, 9 b-a spray drying chamber II, 10 a-a collection bag I, 10 b-a collection bag III, 11 a-a collection bag II, 11 b-a collection bag IV, 12 a-an air cylinder I, 12 b-an air cylinder II, 13-an exhaust valve I, 14-an exhaust valve II, 15-an induced draft fan, 16 a-a fluidization granulation chamber I, 16 b-fluidized granulation chamber two, 17 a-acidic tablet raw material granulation system housing, 17 b-alkaline tablet raw material granulation system housing, 18 a-filtration chamber one, 18 b-filtration chamber two, 19-raw material tank one, 20-raw material tank two, 21-raw material tank three, 22-raw material tank four, 23 a-air pipeline one, 23 b-air pipeline three, 24 a-air pipeline two, 24 b-air pipeline four, 25 a-liquid mixer one, 25 b-liquid mixer two, 26 a-metering pump one, 26 b-metering pump four, 27 a-metering pump two, 27 b-metering pump five, 28 a-metering pump three, 28 b-metering pump six, 29-solution one liquid inlet pipeline, 30 liquid inlet bell mouth, 31-shower head one, etc, 32-a liquid inlet pipe of the second solution, 33-an inner annular wall of the liquid mixing area, 34-a liquid inlet pipeline of the third solution, 35-the liquid mixing area, 36-a second shower nozzle, 37-a liquid outlet bell mouth and 38-a liquid outlet.
Detailed Description
A six-root tea product production system is implemented as follows:
as shown in fig. 1-2, a six-root qing tea product production system comprises: the system comprises an acidic tablet raw material granulating system, an alkaline tablet raw material granulating system, an air inlet system, an air exhaust system and a raw material storing and distributing system;
the acidic tablet raw material granulating system comprises an air flow distribution plate I5 a and an acidic tablet raw material granulating system shell 17a, the lower portion of the air flow distribution plate I5 a is connected with an air duct I4 a, the air flow distribution plate I5 a is connected with the lower portion of the acidic tablet raw material granulating system shell 17a, a fluidized granulating chamber I6 a, a spray drying chamber I9 a and a filter chamber I18 a are sequentially arranged in the acidic tablet raw material granulating system shell 17a from bottom to top, a trapping bag I10 a and a trapping bag II 11a are arranged on the upper portion of the filter chamber I18 a, an air cylinder I12 a is externally connected with the trapping bag I10 a and the trapping bag II 11a, and the lower portion of the filter chamber I18 a is connected to the raw material storing and distributing system through a nozzle I8; the top of the first filtering chamber 18a is connected with the exhaust system through a pipeline;
the alkaline tablet raw material granulating system comprises an air flow distribution plate II 5b and an alkaline tablet raw material granulating system shell 17b, the lower part of the air flow distribution plate II 5b is connected with an air duct II 4b, the air flow distribution plate II 5b is connected with the lower part of the alkaline tablet raw material granulating system shell 17b, a fluidized granulating chamber II 6b, a spray drying chamber II 9b and a filter chamber II 18b are sequentially arranged in the alkaline tablet raw material granulating system shell 17b from bottom to top, a trapping bag III 10b and a trapping bag IV 11b are arranged at the upper part of the filter chamber II 18b, an air cylinder II 12b is externally connected with the trapping bag III 10b and the trapping bag IV 11b, and the lower part of the filter chamber II 18b is connected to the raw material storing and distributing system through a nozzle II 8; the top of the second filtering chamber 18b is connected with the exhaust system through a pipeline;
the air inlet system comprises an air filter 1 and a heater 2 connected with the air filter 1, wherein the heater 2 is connected to a first air channel 4a through a first air door 3a and is connected to a second air channel 4b through a second air door 3 b;
the exhaust system comprises an induced draft fan 15, an exhaust valve I13 and an exhaust valve II 14, the induced draft fan 15 is connected with a filter chamber I18 a through the exhaust valve I13, and the induced draft fan 15 is connected with a filter chamber II 18b through the exhaust valve II 14;
the raw material storage and distribution system comprises a first raw material tank 19, a second raw material tank 20, a third raw material tank 21 and a fourth raw material tank 22, wherein the first raw material tank 19, the second raw material tank 20 and the third raw material tank 21 are connected to a first nozzle 8a through a first pipeline liquid mixer 25a, and a first metering pump 26a, a second metering pump 27a and a third metering pump 28a are sequentially arranged among the first raw material tank 19, the second raw material tank 20, the third raw material tank 21 and the first pipeline liquid mixer 25 a; the second raw material tank 20, the third raw material tank 21 and the fourth raw material tank 22 are connected to the second nozzle 8b through a second liquid mixer 25 b; a metering pump IV 26b, a metering pump V27 b and a metering pump VI 28b are sequentially arranged among the raw material tank II 20, the raw material tank III 21, the raw material tank IV 22 and the liquid mixer II 25 b.
As shown in fig. 2, the first liquid mixer 25a and the second liquid mixer 25b have the same specification, and each liquid mixer includes an annular liquid mixing region 35, an inner annular wall 33 of the annular liquid mixing region, a first shower nozzle 31, a second shower nozzle 36, a second solution inlet pipeline 32, and a third solution inlet pipeline 34, one end of the annular liquid mixing region 35 is provided with a liquid inlet bell mouth 30, and the opposite end of the liquid inlet bell mouth 30 is provided with a liquid outlet bell mouth 37; the second solution inlet pipeline 32 penetrates through an inner annular wall 33 of the annular liquid mixing zone, the first shower nozzle 31 is arranged at one end, opposite to the first solution inlet bell mouth 30, of the second solution inlet pipeline 32, and the first solution inlet bell mouth 30 is connected with a first solution inlet pipeline 29; three inlet line 34 of solution run through the interior rampart 33 of annular liquid mixing district 35, two 36 settings of shower nozzle are in the three inlet line 34 of solution one end of relative play liquid horn mouth 37, play liquid horn mouth 37 leads to liquid outlet 38, and to liquid mixer 25a, the raw materials in raw materials jar 19, raw materials jar two 20, raw materials jar three 21 are solution one, solution two, solution three respectively, and is the same, and to liquid mixer two 25, the raw materials in raw materials jar two 20, raw materials jar three 21, raw materials jar four 22 are solution one, solution two, solution three respectively, and solution one mixes with solution two after liquid inlet horn mouth 30 mixes with solution three again at play liquid horn mouth 37.
The first air door 3a and the second air door 3b are opened and closed periodically, when the first air door 3a is opened, the second air door 3b is closed, the second air cylinder 12b pumps compressed air to the third trapping bag 10b and the fourth trapping bag 11b in the second filtering chamber 18b through pipelines, particles attached to the third trapping bag 10b and the fourth trapping bag 11b in the second filtering chamber 18b are shaken into the second fluidized granulation chamber 6b and can be taken out from the second discharge port 7b periodically, and conversely, the second air door 3b is opened, the first air door 3a is closed, the first air cylinder 12a pumps compressed air to the third trapping bag 10b and the fourth trapping bag 11b in the first filtering chamber 18a through pipelines, and the particles attached to the first trapping bag 10a and the second trapping bag 11a in the first filtering chamber 18a are shaken into the first fluidized granulation chamber 6a and can be taken out from the first discharge port 7a periodically. The acid tablet component and the alkali tablet component are separately collected, so that the consumption caused by acid-base neutralization reaction between organic acid in the acid tablet and inorganic base in the alkali tablet can be avoided.
The working principle of the production system of the six-root tea product is as follows: liquid in the first raw material tank 19, the second raw material tank 20 and the third raw material tank 21 obtained in the sixth step is conveyed into a first liquid mixer 25a in proportion through a first metering pump 26a, a second metering pump 27a and a third metering pump 28a, mixed and then pressurized by compressed air in an air pipeline 23a and an air pipeline 24a, and conveyed to a first nozzle 8a, liquid in the second raw material tank 20, the third raw material tank 21 and the fourth raw material tank 22 obtained in the sixth step is conveyed into a second liquid mixer 25b in proportion through a fourth metering pump 26b, a fifth metering pump 27b and a sixth metering pump 28b, mixed and then pressurized by compressed air in an air pipeline three 23b and an air pipeline four 24b, and then conveyed to a second nozzle 8 b;
air is sucked under negative pressure, passes through the air filter 1 and then is heated by the heater 2, is sent to the first air supply channel 4a through the first air door 3a, is sent to the first air supply channel 4a through the second air door 3b, enters the first fluidized granulation chamber 6a from the first air flow distribution plate 5a, is used for stirring and suspending the seed powder contained in the first air flow distribution plate into fluidization and mixing, enters the second fluidized granulation chamber 6b from the second air flow distribution plate 5b, is used for stirring and suspending the seed powder contained in the first air flow distribution plate into fluidization and mixing;
the liquid material is sent to a first nozzle 8a from a first raw material tank 19, a second raw material tank 20 and a third raw material tank 21, is sent to a second nozzle 8b from the second raw material tank 20, the third raw material tank 21 and a fourth raw material tank 22, is atomized into fine liquid drops by compressed air, one part of the fine liquid drops is used as wetting adhesive to be sprayed on the powder fluidized in the first fluidized bed granulating chamber 6a and the second fluidized granulating chamber 6b to be cemented into a mass for granulating, and the other part of the fine liquid drops is dried by ascending hot air flow and is brought to a first filtering chamber 18a and a second filtering chamber 18 b;
the temperature of the airflow passing through the first fluidized bed granulation chamber 6a and the second fluidized bed granulation chamber 6b is sharply reduced, at the moment, the auxiliary fan blows hot airflow around the nozzle through the blast pipe, the airflow rises along the spray drying chamber under the suction force of the induced draft fan 15, and therefore the temperatures of the spray drying chamber and the filter chamber are increased, and fine liquid drops brought to the first filter chamber 18a and the second filter chamber 18b along with the airflow are fully dried;
the dried powder is captured by the first capture bag 10a and the third capture bag 10b, after a certain amount is reached, the first damper 3a is closed, the second damper 3b is opened, and meanwhile, the first air cylinder 12a pumps compressed air to the first capture bag 10a and the second capture bag 11a in the first filter chamber 18a through pipelines, so that particles attached to the first capture bag 10a and the second capture bag 11a in the first filter chamber 18a are shaken out into the first fluidized granulation chamber 6a and can be periodically taken out from the first discharge port 7 a; on the contrary, when the first damper 3a is opened, the second damper 3b is closed, and the second cylinder 12b pumps compressed air to the third trapping bag 10b and the fourth trapping bag 11b in the second filtering chamber 18b through the pipeline, so that the particles attached to the third trapping bag 10b and the fourth trapping bag 11b in the second filtering chamber 18b are shaken to fall into the second fluidized granulation chamber 6b, and can be periodically taken out from the second discharge port 7b, thereby completing the whole spray drying granulation operation.
Claims (5)
1. A six-root tea-cleaning product production system is characterized in that: the system mainly comprises an acidic tablet raw material granulating system, an alkaline tablet raw material granulating system, an air inlet system, an air exhaust system and a raw material storing and distributing system; the main links of the production system are specifically characterized as follows:
the acidic tablet raw material granulating system comprises a first air flow distribution plate (5a) and a first acidic tablet raw material granulating system shell (17a), wherein the lower part of the first air flow distribution plate (5a) is connected with a first air duct (4a), the first air flow distribution plate (5a) is connected with the lower part of the first acidic tablet raw material granulating system shell (17a), a first fluidized granulating chamber (6a), a first spray drying chamber (9a) and a first filtering chamber (18a) are sequentially arranged in the first acidic tablet raw material granulating system shell (17a) from bottom to top, a first trapping bag (10a) and a second trapping bag (11a) are arranged on the upper part of the first filtering chamber (18a), a first air cylinder (12a) is externally connected with the first trapping bag (10a) and the second trapping bag (11a), and the lower part of the first filtering chamber (18a) is connected to the raw material storing and distributing system through; the top of the first filtering chamber (18a) is connected with the exhaust system through a pipeline;
the alkaline tablet raw material granulating system comprises an air flow distribution plate II (5b) and an alkaline tablet raw material granulating system shell (17b), the lower part of the air flow distribution plate II (5b) is connected with an air duct II (4b), the air flow distribution plate II (5b) is connected with the lower part of the alkaline tablet raw material granulating system shell (17b), a fluidized granulating chamber II (6b), a spray drying chamber II (9b) and a filter chamber II (18b) are sequentially arranged in the alkaline tablet raw material granulating system shell (17b) from bottom to top, a trapping bag III (10b) and a trapping bag IV (11b) are arranged on the upper part of the filter chamber II (18b), an air cylinder II (12b) is externally connected with the trapping bag III (10b) and the trapping bag IV (11b), and the lower part of the filter chamber II (18b) is connected to the raw material storing and distributing system through a nozzle II (; the top of the second filtering chamber (18b) is connected with the exhaust system through a pipeline;
the air inlet system comprises an air filter (1) and a heater (2) connected with the air filter (1), wherein the heater (2) is connected to a first air channel (4a) through a first air door (3a) and is connected to a second air channel (4b) through a second air door (3 b);
the exhaust system comprises an induced draft fan (15), a first exhaust valve (13) and a second exhaust valve (14), the induced draft fan (15) is connected with the first filter chamber (18a) through the first exhaust valve (13), and the induced draft fan (15) is connected with the second filter chamber (18b) through the second exhaust valve (14);
the raw material storage and distribution system comprises a first raw material tank (19), a second raw material tank (20), a third raw material tank (21) and a fourth raw material tank (22), wherein the first raw material tank (19), the second raw material tank (20) and the third raw material tank (21) are connected to a first nozzle (8a) through a first pipeline liquid mixer (25a), and a first metering pump (26a), a second metering pump (27a) and a third metering pump (28a) are sequentially arranged among the first raw material tank (19), the second raw material tank (20), the third raw material tank (21) and the first liquid mixer (25 a); the second raw material tank (20), the third raw material tank (21) and the fourth raw material tank (22) are connected to the second nozzle (8b) through a second liquid mixer (25 b); a metering pump four (26b), a metering pump five (27b) and a metering pump six (28b) are sequentially arranged between the raw material tank II (20), the raw material tank III (21), the raw material tank IV (22) and the liquid mixer II (25 b).
2. The six-root tea-cleaning product production system according to claim 1, wherein the first damper (3a) and the second damper (3b) are periodically opened and closed, when the first damper (3a) is opened, the second damper (3b) is closed, and the second air cylinder (12b) pumps out compressed air to the third trapping bag (10b) and the fourth trapping bag (11b) in the second filtering chamber (18b) through the duct, thereby shaking the particles attached to the third trapping bag (10b) and the fourth trapping bag (11b) in the second filtering chamber (18b) into the second fluidized granulating chamber (6b), and periodically taking out the particles from the second outlet (7b), whereas, when the second damper (3b) is opened, the first damper (3a) is closed, and the first air cylinder (12a) pumps out compressed air to the third trapping bag (10b) and the fourth trapping bag (11b) in the first filtering chamber (18a) through the duct, the particles attached to the first trapping bag (10a) and the second trapping bag (11a) in the first filtering chamber (18a) are shaken into the first fluidized granulating chamber (6a), and can be periodically taken out from the first discharging port (7 a).
3. The six-root tea cleaning product production system according to claim 1, wherein the first liquid mixer (25a) and the second liquid mixer (25b) have the same specification, and each liquid mixer comprises an annular liquid mixing area (35), an inner annular wall (33) of the annular liquid mixing area, a first shower nozzle (31), a second shower nozzle (36), a second solution inlet pipeline (32) and a third solution inlet pipeline (34), wherein one end of the annular liquid mixing area (35) is provided with a liquid inlet bell mouth (30), and the other end of the liquid inlet bell mouth (30) is provided with a liquid outlet bell mouth (37); the second solution inlet pipeline (32) penetrates through an inner annular wall (33) of the annular liquid mixing zone, the first shower nozzle (31) is arranged at one end, opposite to the first solution inlet pipeline (30), of the second solution inlet pipeline (32), and the first solution inlet pipeline (29) is connected to the first solution inlet pipeline (30); three inlet lines of solution (34) run through interior rampart (33) in annular liquid mixing district (35), shower nozzle two (36) set up the one end of three inlet lines of solution (34) relative play liquid horn mouth (37), go out liquid horn mouth (37) and lead to liquid outlet (38), to liquid mixing ware (25a), the raw materials in feed tank one (19), feed tank two (20), feed tank three (21) are solution one, solution two, solution three respectively, and is the same, to liquid mixing ware two (25b), feed tank two (20), feed tank three (21), the raw materials in feed tank four (22) are solution one, solution two, solution three respectively, and solution one mixes with solution three after liquid inlet horn mouth (30) mixes again with solution three in play liquid horn mouth (37).
4. The six-root tea-cleaning product production system according to claim 3, wherein the first shower head (31) and the second shower head (36) are both spherical shower heads and are provided with a plurality of liquid outlet through holes.
5. The system for producing a six-root qing tea product according to claim 1, wherein the flow rates of the first metering pump (26a), the second metering pump (27a), the third metering pump (28a), the fourth metering pump (26b), the fifth metering pump (27b) and the sixth metering pump (28b) are adjustable, that is, the mixing ratio of the liquid introduced into the first liquid mixer (25a) and the second liquid mixer (25b) is adjustable.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020495933.3U CN212911502U (en) | 2020-04-08 | 2020-04-08 | Six clear tea goods production systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020495933.3U CN212911502U (en) | 2020-04-08 | 2020-04-08 | Six clear tea goods production systems |
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