CN201770693U - Control system for beer saccharification production process - Google Patents

Control system for beer saccharification production process Download PDF

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Publication number
CN201770693U
CN201770693U CN2010202948097U CN201020294809U CN201770693U CN 201770693 U CN201770693 U CN 201770693U CN 2010202948097 U CN2010202948097 U CN 2010202948097U CN 201020294809 U CN201020294809 U CN 201020294809U CN 201770693 U CN201770693 U CN 201770693U
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China
Prior art keywords
control system
valve
central processing
processing unit
production process
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Expired - Fee Related
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CN2010202948097U
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Chinese (zh)
Inventor
张丰
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JINAN HELISHI AUTOMATION CO Ltd
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JINAN HELISHI AUTOMATION CO Ltd
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Priority to CN2010202948097U priority Critical patent/CN201770693U/en
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Abstract

The utility model discloses a control system for a beer saccharification production process. The control system controls temperature of a saccharification boiler, dynamic low-pressure boiling of a wort boiler and heat energy recovery, and comprises a data monitoring and acquisition system, an electric control system and a central control system, wherein the data monitoring and acquisition system realizes acquisition of simulation information and equipment state; the electric control system realizes control over a motor and a valve; and the central control system realizes historical data filing and parameter input and modification. A control method for the beer saccharification production process provided by the utility model has the advantages that: 1, the entire beer saccharification production process is automatically and accurately controlled, is easy to adjust and saves labor by arranging a hierarchical control system; and 2, by setting the dynamic low-pressure boiling process and the heat energy recovery process, the product quality is improved, the resource waste is prevented and the resource is saved.

Description

A kind of Controlling System that is used for the beer saccharification production process
Technical field
The utility model relates to beer saccharification production control field, specifically be a kind ofly be used for beer saccharification production process brew kettle temperature, the boiling pot dynamic low voltage boils and the Controlling System of energy recovery etc.
Background technology
At present, in the beer saccharification production process, kettle temperature pressure adopts the mode that the numerical control table shows and manually-operated gate is controlled mostly, specifically be to come by-pass valve control or by-pass valve control manually with numerical control table collecting temperature data, to regulate the temperature in the pot, low, the poor anti jamming capability of this kind control mode precision, and the process data modification is complicated, and shortcoming is obvious.In addition, the pot body adopts the single hop temperature control, promptly has only a cover regulated valve, easily causes pot interior wheat juice to be heated inhomogeneous.In addition present domestic most of brew-house still adopts traditional boiling process, boils the intensity height, and heat energy consumption is big, not only influences beer quality, and the secondary steam of discharging in the boiling part takes away a large amount of heats and do not recycle, and is wasted in a large number.
Summary of the invention
At the problems referred to above, the utility model provides a kind of Controlling System of controlling the beer saccharification production process of accurate, energy-conservation, easy handling.
A kind of Controlling System that is used for the beer saccharification production process comprises brew kettle temperature, boiling pot dynamic low voltage is boiled and energy recovery control, comprising:
Realize gathering the data monitoring and the acquisition system of analog quantity information and equipment state, realize the electric control system of electric motor, valve control and realize the master control system that historical data archiving, parameter input are revised, wherein,
Data monitoring and acquisition system comprise data acquisition module, and the input terminus of data acquisition module is connected with various transmitters such as position transducer, hot resistance, pressure unit, fluid level transmitter, and the output terminal of data acquisition module is connected to master control system; The positional information of position transducer perception valve, hot resistance sense temperature information, pressure unit detecting pressure information, fluid level transmitter detects boiling pot liquid level and brew kettle liquid level information, be transferred to data acquisition module respectively, be transferred to master control system by data acquisition module again, realize the monitoring and the collection of data;
Electric control system comprises electric motor loop, valve loop, power supply, and is connected respectively to master control system; Realize control by electric motor loop, valve loop, realize power supply by the control power supply to motor and valve;
Master control system comprises central processing unit, central processing unit is connected with industrial computer, touch-screen, industrial computer connects electric motor loop, valve loop and the power supply of master control system respectively, realization is to the control of motor, valve, thereby realize control, and central processing unit connects data acquisition module to boiling pot pressure, brew kettle temperature and boiling pot energy recovery; Touch-screen can be realized man-machine interaction, and for example touch-screen can be provided with data such as high-low pressure value in the boiling pot, time.
Further, described brew kettle temperature control is such: be provided with temperature sensor in the brew kettle, temperature sensor arrives central processing unit by data acquisition module with data transmission, central processing unit is realized the brew kettle temperature controlling through the motor and the valve of industrial computer control brew kettle by the running of control motor and the switch of valve.
Further, described boiling pot dynamic low voltage boils pressure-controlling and energy recovery is such: boiling pot is provided with pressure unit and fluid level transmitter, valve is provided with position transducer, pressure unit, fluid level transmitter and position transducer arrive central processing unit by data acquisition module with data transmission, and central processing unit is by the motor and the valve of industrial computer control boiling pot; And the boiling pot steam output end is connected with an energy recovery jar that has a temperature sensor, the energy recovery jar is provided with a water inlet and a water outlet, water inlet and water outlet are provided with valve, water inlet is connected to water supply pump, water outlet is connected to hot water pump, and central processing unit is by industrial computer by-pass valve control, water supply pump and hot water pump.
Further, hot water pump is connected with energy storage canister, receives the effusive hot water of water outlet, and promptly the thermal source of Hui Shouing can be used for uses such as wheat juice preheating.
For boiling pot, control the pressure in the boiling pot, need by the open cold water pump, make water supply pump take out the steam that cold water enters energy recovery jar cooling the inside, thereby reduce the interior pressure of boiling pot, flow into energy storage canister through hot water pump, can be used as uses such as wheat juice preheating through steam-heated water, thereby realize that dynamic low voltage boils pressure-controlling, also realized energy recovery.
The control method of the beer saccharification production process that the utility model provides has following advantage:
1, by the fractionated Controlling System is set, realize the automatic control to whole beer saccharification production process, control precisely is easy to regulate, and saves manpower.
2, be provided with and dynamically boil and the process of energy recovery, improved quality product, avoided the waste of resource, saved resource.
Description of drawings
Fig. 1 is the electrical schematic diagram of the utility model embodiment;
Fig. 2 is the structural representation of the utility model energy recovery;
Fig. 3 is that the utility model boiling pot dynamic low voltage boils pressure controlled synoptic diagram.
Embodiment
Embodiment with indefiniteness further explains, illustrates the technical program below.
A kind of Controlling System that is used for the beer saccharification production process, as shown in Figure 1, realization is to brew kettle temperature, boiling pot pressure, the control of boiling pot energy recovery, comprise: data monitoring and acquisition system 1 that various transmitters 4, transmitter 5 and data acquisition module 6 and field instrument etc. constitute, the electrical apparatus control system 2 that electric motor loop 7, valve loop 8 and power supply 9 and variable frequency control etc. constitute, and the master control system 3 of central processing unit 10 and industrial computer 11 and touch-screen 12 formations.
Control is such for the brew kettle temperature: be provided with temperature sensor in the brew kettle, temperature sensor arrives central processing unit by data acquisition module with data transmission, central processing unit is realized the brew kettle temperature controlling through the motor and the valve of industrial computer control brew kettle by the running of control motor and the switch of valve.
Boil pressure-controlling and energy recovery is such for the boiling pot dynamic low voltage: as shown in Figure 2, boiling pot 13 is provided with pressure unit and fluid level transmitter, valve is provided with position transducer, pressure unit, fluid level transmitter and position transducer arrive central processing unit by data acquisition module with data transmission, and central processing unit is by the motor and the valve of industrial computer control boiling pot; And the boiling pot steam output end is connected with an energy recovery jar 14 that has a temperature sensor, energy recovery jar 14 is provided with a water inlet and a water outlet, water inlet and water outlet are provided with valve, water inlet is connected to water supply pump, water outlet is connected to hot water pump, central processing unit is by industrial computer by-pass valve control, water supply pump and hot water pump, and hot water pump connects an energy storage canister 15, the storage hydro-thermal.
Specifically, realize that the boiling pot dynamic low voltage boils pressure controlled process as shown in Figure 3, for boiling pot, by precooking and boosting process, reach a certain force value, control the pressure in the boiling pot, need by the open cold water pump, make water supply pump take out the steam that cold water enters energy recovery jar cooling the inside, thereby reduce the interior pressure of boiling pot, i.e. step-down process, flow into energy storage canister through steam-heated water through hot water pump, promptly realize the pressure in the boiling pot is had the process of continuous lifting, thereby realize that dynamic low voltage boils pressure-controlling, also realized energy recovery by the work of water supply pump and hot water pump.

Claims (4)

1. a Controlling System that is used for the beer saccharification production process comprises brew kettle temperature, boiling pot dynamic low voltage is boiled and energy recovery control, it is characterized in that comprising:
Realize gathering the data monitoring and the acquisition system of analog quantity information and equipment state, realize the electric control system of electric motor, valve control and realize the master control system that historical data archiving, parameter input are revised, wherein,
Data monitoring and acquisition system comprise data acquisition module, and the input terminus of data acquisition module is connected with position transducer, hot resistance, pressure unit, fluid level transmitter, and the output terminal of data acquisition module is connected to master control system;
Electric control system comprises electric motor loop, valve loop, power supply, and is connected respectively to master control system;
Master control system comprises central processing unit, and central processing unit is connected with industrial computer, touch-screen, and industrial computer connects electric motor loop, valve loop and the power supply of master control system respectively, and central processing unit connects data acquisition module.
2. the Controlling System that is used for the beer saccharification production process according to claim 1, it is characterized in that: described brew kettle temperature control is such: be provided with temperature sensor in the brew kettle, valve is provided with position transducer, temperature sensor and position transducer arrive central processing unit by data acquisition module with data transmission, and central processing unit is through the motor and the valve of industrial computer control brew kettle.
3. the Controlling System that is used for the beer saccharification production process according to claim 1, it is characterized in that: described boiling pot dynamic low voltage boils pressure-controlling and energy recovery is such: boiling pot is provided with pressure unit and fluid level transmitter, valve is provided with position transducer, pressure unit, fluid level transmitter and position transducer arrive central processing unit by data acquisition module with data transmission, and central processing unit is by the motor and the valve of industrial computer control boiling pot; And the boiling pot steam output end is connected with an energy recovery jar that has a temperature sensor, the energy recovery jar is provided with a water inlet and a water outlet, water inlet and water outlet are provided with valve, water inlet is connected to water supply pump, water outlet is connected to hot water pump, and central processing unit is by industrial computer by-pass valve control, water supply pump and hot water pump.
4. the Controlling System that is used for the beer saccharification production process according to claim 3 is characterized in that: described hot water pump is connected with an energy storage canister, and energy storage canister receives through the effusive hot water of water outlet.
CN2010202948097U 2010-08-18 2010-08-18 Control system for beer saccharification production process Expired - Fee Related CN201770693U (en)

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CN2010202948097U CN201770693U (en) 2010-08-18 2010-08-18 Control system for beer saccharification production process

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Application Number Priority Date Filing Date Title
CN2010202948097U CN201770693U (en) 2010-08-18 2010-08-18 Control system for beer saccharification production process

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102426468A (en) * 2011-12-01 2012-04-25 西安中轻造纸机械集团有限公司 Controller of saccharifying instrument
CN107102086A (en) * 2017-06-24 2017-08-29 深圳源广安智能科技有限公司 A kind of Beer Brewage material quality evaluation system
CN111913432A (en) * 2020-08-31 2020-11-10 深圳技术大学 Beer brewing control system and method
CN114369507A (en) * 2022-01-28 2022-04-19 中国轻工业广州工程有限公司 Automatic control system and method for brewing beer saccharification process

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102426468A (en) * 2011-12-01 2012-04-25 西安中轻造纸机械集团有限公司 Controller of saccharifying instrument
CN107102086A (en) * 2017-06-24 2017-08-29 深圳源广安智能科技有限公司 A kind of Beer Brewage material quality evaluation system
CN111913432A (en) * 2020-08-31 2020-11-10 深圳技术大学 Beer brewing control system and method
CN114369507A (en) * 2022-01-28 2022-04-19 中国轻工业广州工程有限公司 Automatic control system and method for brewing beer saccharification process
CN114369507B (en) * 2022-01-28 2024-09-13 中国轻工业广州工程有限公司 Automatic control system and method for saccharification process of refined beer

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Granted publication date: 20110323

Termination date: 20130818