Summary of the invention
The shortcomings that for the above-mentioned prior art or deficiency, the technical problem to be solved in the present invention is to provide a kind of process tank and
Processing method, compact, operating cost are low, easy to operate, starting reaction is fast, stops rapidly, can be with with opening.
In order to solve the above technical problems, the present invention has following constitute:
Including tank body, left end cap and right end cap, the motor and stirring group of the tank body two sides is arranged in a kind of process tank
Part;The tank body is equipped with inlet port and outlet port;The mixing component includes the shaft being arranged in the tank body, and described turn
Axis connect with the motor and rotates under the driving effect of the motor;Multiple mixing parts are additionally provided in the shaft.
Axially staggered laying of the mixing part along the shaft.
The mixing part is rake plow structure.
It circumferentially lays in the same direction at the tip end of the rake plow structure.
Sampler is additionally provided on the tank body.
The sampler includes sampling bottle, ball valve, handle and negative pressure gas flow interface, and the ball valve passes through a fixed ring
It is mounted on the sampling bottle, the handle is connect with the ball valve, and the negative pressure gas flow interface setting connecting with negative pressure device exists
On the sampling bottle.
Pneumostome and drain are additionally provided on the tank body.
Steam port and condensation-water drain are additionally provided on the tank body, the upside of the tank body, institute is arranged in the steam port
State the downside that the tank body is arranged in condensation-water drain.
At least one sensor for measuring temperature is additionally provided on the tank body.
The surface of the tank body is additionally provided with insulating layer.
Using the processing method of the process tank, steps are as follows: S1 ginseng is matched, and carries out automatic sampling according to a certain percentage;S2
Sweetening, addition higher boiling feed liquid carry out sweetening processing;S3 sterilizing carries out high-temperature sterilization processing using steam;S4 is cooling;S5 soda acid
It adjusts, addition pH adjusts the pH that liquid adjusts material;S6 discharging.
The processing method further includes bis- sweetenings of S51, adds sucrose and sweetener and carries out to the intracorporal material of the tank
Secondary sweetening.
The processing method further includes S52 blending, is carried out at blending by addition essence to the intracorporal material of the tank
Reason.
Compared with prior art, the present invention has the following technical effect that
The present invention is stirred the intracorporal material of tank using rake plow structure, due to harrowing the unique pointed nose structure of plow structure
The bonding even agglomeration etc. that can be sufficiently stirred to be uniformly mixed to the intracorporal material of tank, and not will lead to material, is suitable for tool
There is the stirring of the buccal cigarette tobacco powder material of certain humidity;
Sampling apparatus realizes that structure is simple to the automatic sampling of buccal cigarette tobacco powder material using negative pressure in the present invention, operation
It is convenient, inspect sample in tank by random samples at any time with can be convenient.
Specific embodiment
It is described further below with reference to technical effect of the attached drawing to design of the invention, specific structure and generation, with
It is fully understood from the purpose of the present invention, feature and effect.
As depicted in figs. 1 and 2, including tank body 10, the left end caps of 10 two sides of tank body is arranged in the present embodiment process tank
20 and right end cap 30, motor 40 and mixing component 50;The tank body 10 is equipped with feed inlet 11 and discharge port 12;The stirring
Component 50 includes the shaft 51 being arranged in the tank body 10, and the shaft 51 connect with the motor 40 and in the motor 40
Driving effect under rotate;Multiple mixing parts 52 are additionally provided in the shaft 51.The present embodiment compact, operating cost are low,
It is easy to operate, starting reaction is fast, stops rapidly, can be with with opening.
The maximum heating temperature of the present embodiment process tank requires to reach 150 degrees Celsius, and type of production process tank is usually less than
120 degrees Celsius, common process tank is difficult to meet the technical requirements of the present embodiment.The present embodiment process tank, which uses, has pressure vessel
The manufacture material and stainless steel material authenticated through safety detection is made, meets food safety grade, and be miscellaneous by food safety
The high-quality stainless steel 304 of quality detection, design work pressure are 0.7Mpa, and tank body heating reaches 150 degrees Celsius or more.
The surface of the tank body 10 is additionally provided with insulating layer.The present embodiment uses collet heating method, not only increases Double-layer clamp
Stress levels are covered, the mesh that insulating layer (stainless steel heat preservation jacket) is totally-enclosed, and not only realization heat preservation energy-saving lowers consumption is equipped with outside collet
, and more preferably guarantee personnel's safe operation.
The present embodiment also configures the control system there are three types of control model, specifically:
(i) automatic control mode: control system works out processing technology ginseng under automated manner, through touch screen operation panel
Number, starting is by automatic control program, fully automatic operation heating temperature curve, and presetting mixing component work pace, (such as setting is every
One hour stirs 15 minutes, revolving speed 40RPM etc.), one time sweetening automatic ration feeds, cooling curve, and secondary sweetening is automatically fixed
Amount charging, sampling pH, water content detection are reminded, and pH value adjusts the charging of liquid automatic ration, and self-emptying is automatic to clean, automatic to dry
Whole processes such as sterilizing;Further include motor open/stop, troubleshooting (sound-light alarm etc.), the movement of executing agency and necessary
Manual operation function etc. under auto state;Meanwhile the processes such as temperature, pressure, moisture, flow for acquiring material and relevant device
Technological parameter is finally met the requirement of each technological parameter by the control variable of certain algorithm regulating loop.Each equipment on startup,
Should be according to the opposite direction sequence starting of Flow of Goods and Materials, starting separated in time between every neighbouring device has observing and controlling component
Equipment, running order determines according to the production process, with Anti-blockage, reduces equipment and starts impact to power grid.
(ii) single machine control model: control system provides single-set operation function, and realization manually opens each equipment motor
The function of move/stopping operation facilitates the maintenance of equipment.
(iii) lock-in control mode: under lock-in control mode, system, which enters, forbids control model, all motor,
Solenoid valve, regulating valve forcibly be in power failure state, all motors, solenoid valve and other control devices no matter pass through scene or
" starting " in operator control panel cannot all start.
Steam port 16 and condensation-water drain 17 are additionally provided on the tank body 10, the steam port 16 is arranged in the tank body 10
Upside, the downside of the tank body 10 is arranged in the condensation-water drain 17.Steam is conveyed into tank body 10 by steam port 16,
It realizes that steam injection directly heats, tank body 10 can not only be made to heat up rapidly, shorten preheating time, it is energy-saving, also make this
This process tank, which removes, can press the manufacturing process development of U.S.'s buccal cigarette, moreover it is possible to produce Sweden's Gothix technique (using steam injection heating)
Mouth containing tobacco product, improve the product development of pilot scale line ability and flexibility.
Meanwhile the condensation-water drain 17 can also be used as the water inlet of cooling system, the steam port 16 also can be used as cold
But the water outlet of system.
The sensor for measuring temperature 18 for the actual temperature that at least one is used to measure material is additionally provided on the tank body 10.This
In embodiment, the sensor for measuring temperature 18 is preferably arranged to two, and (one group of temperature measurement is sensed more than common process tank
Device), material practicable process temperature can be more accurately grasped, and tank body thermometric is only transmitted to measure technological temperature indirectly.
In the present embodiment, the tank body 10 is mounted in mounting bracket, and is further provided between the tank body and bracket
Four high-precision weighing sensors, the high-precision weighing sensor can carry out dynamic weighing to tank body in real time, even if stirring
Component operating nor affects on precision, and operator can understand the weight change situation in tank by display screen at any time, improve and add
The control ability of work technique, for buccal cigarette technical study process control provide can dynamic connection survey grasp technical conditions.
Pneumostome 14 and drain 15 are additionally provided on the tank body 10.
It is additionally provided with door 19 on the tank body 10, is additionally provided with safety switch on the door 19.
Further, gauge port a, relief valve port b and spare mouth c are additionally provided on the tank body 10.
The present embodiment process tank is also configured with automatic cleaning system, the spray assemblies being oppositely arranged using both ends: has
Line realizes the function of cleaning automatically.
The present embodiment process tank is also configured with blow-dry device, is quickly dried up by compressed air to the tank body after cleaning
Processing.
As shown in Figure 3 and Figure 4, the mixing part 52 is along the axially staggered laying of the shaft 51, further, the stirring
Portion 52 is rake plow structure, and the intracorporal material of tank can be sufficiently stirred in the unique pointed nose structure of rake plow structure, and will not
Lead to the bonding even agglomeration etc. of material.Further, the tip end of the rake plow structure is circumferentially laid in the same direction, the laying side
Formula is conducive to preferably be stirred the material of tank body 10.
The sampler 13 being arranged on the tank body 10 as shown in Figures 5 to 7.The sampler 13 includes sampling
Bottle 131, ball valve 132, handle 133 and negative pressure gas flow interface 135, the ball valve 132 are mounted on described by a fixed ring 134
On sampling bottle 131, the handle 133 is connect with the ball valve 132, and the negative pressure gas flow interface 135 connecting with negative pressure device is arranged
On the sampling bottle 131.Ball valve 132 is closed, negative pressure device is connected, so that the sampling bottle 131 is in negative pressure state, then
Ball valve is opened, due to suction function, the material in tank body 10 with certain humidity is gradually adsorbed in sampling bottle 131.
Using the processing method of the process tank, steps are as follows:
S1 ginseng is matched, and carries out automatic sampling, material supplied materials moisture < 20% according to a certain percentage;
S2 sweetening, addition higher boiling feed liquid carry out sweetening processing, and the additive amount of the higher boiling feed liquid is 10% (W/W);
S3 sterilizing carries out high-temperature sterilization processing using steam, and parameters are 80-90 DEG C of temperature under the conditions of steam sterilizing;
Time 6-8h;The revolving speed of motor control shaft is 30rpm;Steam pressure is 6kg/cm2。
S4 is cooling, and the cooling temperature of the step is 24-26 DEG C;The present embodiment is further equipped with forced cooling device, Neng Goushi
It is now quickly cooled down, in the waiting time arrived between flavoring process after the heating process that sterilizes, (common process tank is cold using nature for shortening
But), improve process tank working efficiency and and response speed, improve product quality, and adapt to interruption, continuously-running duty,
It improves experiment work efficiency and technology controlling and process is horizontal.
S5 acid-base accommodation, addition pH adjust the pH that liquid adjusts material, and the additive amount that pH adjusts liquid is 5% (W/W);
Bis- sweetenings of S51 add sucrose and sweetener and carry out secondary sweetening to the material in the tank body 10.Sucrose adds
Dosage is 10% (W/W), and the additive amount of sweetener is 0.6% (W/W).
S52 blending carries out blending processing to the material in the tank body 10 by addition essence, and the additive amount of essence is
4% (W/W).
S6 discharging, by above-mentioned series of processes, is made buccal cigarette finished product, which will enter subsequent processing and carry out finished product
Packing processes.Discharging moisture < 50% of finished product passes through the opening size and optimization structure of big discharge port, it is ensured that 50% moisture object
Material discharging is clean.
The above embodiments are merely illustrative of the technical solutions of the present invention and it is non-limiting, reference only to preferred embodiment to this hair
It is bright to be described in detail.Those skilled in the art should understand that can modify to technical solution of the present invention
Or equivalent replacement should all cover in scope of the presently claimed invention without departing from the spirit and scope of the technical solution of the present invention
It is interior.