The invention discloses a calibrating method for concentrating pan water evaporation quantity. According to the working principle, as the calibrating method for the concentrating pan water evaporation quantity is provided, the purposes of providing the calibrating method used for large-scale concentration equipment, mastering the production capacity of the equipment, completing the design capacity of the equipment and promoting the design level of this type of equipment are achieved.
Description Concentration pan moisture content sends out steaming amount standardizationTechnical field
The present invention relates to field of food, be specifically related to concentration pan moisture content and send out steaming amount standardization.
Background technology
At present in the design and use of our food service industry equipment, there is no concrete, clear and definite, standard, exercisable specification.In actual production, device fabrication producer and user are to feed intake quantity by front operation, with final concentrated after the quantity of finished product, estimate the output of concentration pan.Just there is very big error here, cause the situation that both sides do not approve.Meanwhile, the raw material variety that will carry out processing in food service industry is of a great variety, and its physical property also varies (comprising the viscosity of material, proportion, specific heat, solid content etc.), and the technological process of its pre-treatment processing is had nothing in common with each other.So the demarcation to the actual production capacity of concentration pan, just more difficult, the result finally estimated, is also difficult to the approval obtaining both sides of supply and demand.Therefore, the detection method just needing both sides of supply and demand to admit in reality, demarcates the water evaporates amount of concentration pan.Simultaneously also can be engaged in the slip-stick artist of design effort for us, in careful design and well designed, provide important parameter foundation.Also for equipment acceptance provides call parameter.
Summary of the invention
For solving the problems of the technologies described above, the present invention proposes concentration pan moisture content and send out steaming amount standardization, with reach provide large-scale concentrator is used scaling method, grasp equipment capacity, Improving Equipment designed capacity and promote that the design level of this kind equipment rises to object.
For achieving the above object, technical scheme of the present invention is as follows:
A kind of concentration pan moisture content sends out steaming amount standardization, and its concrete steps are as follows:
1). the preparatory stage:
(1). early stage by equipment debugging installation, comprising assembling, pressure testing, examination steam, be pressurized air, formula motor steering, test various instrument and PLC machine);
(2). one piece of electromagnetic flowmeter of connecting at triple effect feed pipe place, carries out flux cumulating when realizing test;
(3). add water step by step to triple effect concentration pan;
(4). open each effect ebullator step by step;
(5). again adjust the liquid level numerical value of each effect and perform record, (or marking a certain liquid level);
(6). open vacuum pump;
(7). open steam valve, send into steam;
(8). open cold condenser water pump, record water temperature;
(9). adjust the vacuum tightness of each effect, reach setting value;
2). test phase
(1), after the temperature of each effect reaches design temperature, after vacuum tightness also reaches requirement, timing can be started;
(2) after starting timing, along with the operation of concentration pan, can continuous moisturizing.Preferably run more than 6 hours continuously;
(3) perform every record, comprising: respectively imitate vacuum tightness, respectively imitate temperature, vapor pressure, cooling water temperature etc.;
(4) after reaching the test duration, orderly closedown on request;
(5) classified finishing is carried out to all kinds of numerical value, first will perform integrated flow number in flowmeter, its secondary liquid level number recording each effect, then EQUILIBRIUM CALCULATION FOR PROCESS is carried out, just can obtain concentration pan within the unit interval, the evaporation capacity of moisture content, therefore can demarcate the value of concentration pan.
Preferably, the method adopts water as heating medium, carries out simulation production.
Pass through technique scheme, the present invention sends out steaming amount standardization by providing a kind of concentration pan moisture content, reach provide large-scale concentrator is used scaling method, grasp equipment capacity, Improving Equipment designed capacity and promote that the design level of this kind equipment rises to object.
Embodiment
Below the technical scheme in the embodiment of the present invention is clearly and completely described.
The invention provides concentration pan moisture content and send out steaming amount standardization, its principle of work is by providing a kind of concentration pan moisture content to send out steaming amount standardization, reach provide large-scale concentrator is used scaling method, grasp equipment capacity, Improving Equipment designed capacity and promote that the design level of this kind equipment rises to object.
Below in conjunction with embodiment and embodiment, the present invention is further detailed explanation.
A kind of concentration pan moisture content sends out steaming amount standardization, and its concrete steps are as follows:
1). the preparatory stage:
(1). early stage by equipment debugging installation, comprising assembling, pressure testing, examination steam, be pressurized air, formula motor steering, test various instrument and PLC machine);
(2). one piece of electromagnetic flowmeter of connecting at triple effect feed pipe place, carries out flux cumulating when realizing test;
(3). add water step by step to triple effect concentration pan;
(4). open each effect ebullator step by step;
(5). again adjust the liquid level numerical value of each effect and perform record, (or marking a certain liquid level);
(6). open vacuum pump;
(7). open steam valve, send into steam;
(8). open cold condenser water pump, record water temperature;
(9). adjust the vacuum tightness of each effect, reach setting value;
2). test phase
(1), after the temperature of each effect reaches design temperature, after vacuum tightness also reaches requirement, timing can be started;
(2) after starting timing, along with the operation of concentration pan, can continuous moisturizing.Preferably run more than 6 hours continuously;
(3) perform every record, comprising: respectively imitate vacuum tightness, respectively imitate temperature, vapor pressure, cooling water temperature etc.;
(4) after reaching the test duration, orderly closedown on request;
(5) classified finishing is carried out to all kinds of numerical value, first will perform integrated flow number in flowmeter, its secondary liquid level number recording each effect, then EQUILIBRIUM CALCULATION FOR PROCESS is carried out, just can obtain concentration pan within the unit interval, the evaporation capacity of moisture content, therefore can demarcate the value of concentration pan.
By above mode, concentration pan moisture content provided by the present invention sends out steaming amount standardization, by providing a kind of concentration pan moisture content to send out steaming amount standardization, reach provide large-scale concentrator is used scaling method, grasp equipment capacity, Improving Equipment designed capacity and promote that the design level of this kind equipment rises to object.
The above-described preferred implementation being only concentration pan moisture content disclosed in this invention and sending out steaming amount standardization; should be understood that; for the person of ordinary skill of the art; without departing from the concept of the premise of the invention; can also make some changes and improvements, these all belong to protection scope of the present invention.
Claims (2)1. concentration pan moisture content sends out steaming amount standardization, it is characterized in that, its concrete steps are as follows:
1). the preparatory stage:
(1). early stage by equipment debugging installation, comprising assembling, pressure testing, examination steam, be pressurized air, formula motor steering, test various instrument and PLC machine);
(2). one piece of electromagnetic flowmeter of connecting at triple effect feed pipe place, carries out flux cumulating when realizing test;
(3). add water step by step to triple effect concentration pan;
(4). open each effect ebullator step by step;
(5). again adjust the liquid level numerical value of each effect and perform record, (or marking a certain liquid level);
(6). open vacuum pump;
(7). open steam valve, send into steam;
(8). open cold condenser water pump, record water temperature;
(9). adjust the vacuum tightness of each effect, reach setting value;
2). test phase
(1), after the temperature of each effect reaches design temperature, after vacuum tightness also reaches requirement, timing can be started;
(2) after starting timing, along with the operation of concentration pan, can continuous moisturizing.Preferably run more than 6 hours continuously;
(3) perform every record, comprising: respectively imitate vacuum tightness, respectively imitate temperature, vapor pressure, cooling water temperature etc.;
(4) after reaching the test duration, orderly closedown on request;
(5) classified finishing is carried out to all kinds of numerical value, first will perform integrated flow number in flowmeter, its secondary liquid level number recording each effect, then EQUILIBRIUM CALCULATION FOR PROCESS is carried out, just can obtain concentration pan within the unit interval, the evaporation capacity of moisture content, therefore can demarcate the value of concentration pan.
2. concentration pan moisture content according to claim 1 sends out steaming amount standardization, it is characterized in that, the method adopts water as heating medium, carries out simulation production.
CN201410003347.1A 2014-01-03 2014-01-03 Concentration pan moisture content sends out steaming amount standardization Active CN104596597B (en) Priority Applications (1) Application Number Priority Date Filing Date Title CN201410003347.1A CN104596597B (en) 2014-01-03 2014-01-03 Concentration pan moisture content sends out steaming amount standardization Applications Claiming Priority (1) Application Number Priority Date Filing Date Title CN201410003347.1A CN104596597B (en) 2014-01-03 2014-01-03 Concentration pan moisture content sends out steaming amount standardization Publications (2) Family ID=53122531 Family Applications (1) Application Number Title Priority Date Filing Date CN201410003347.1A Active CN104596597B (en) 2014-01-03 2014-01-03 Concentration pan moisture content sends out steaming amount standardization Country Status (1) Citations (6) * Cited by examiner, â Cited by third party Publication number Priority date Publication date Assignee Title CN1038774A (en) * 1988-06-13 1990-01-17 é¿å°æ¯ç¹ç½å§å¼åå¡æ ¹çå ¸å ¬å¸ Liquid method of evaporating and equipment CN1094013A (en) * 1993-03-15 1994-10-26 æ°ä½äº§åä¸åå¦å ¬å¸ Sulfuric acid purifying and concentration technology JPH07174593A (en) * 1993-12-20 1995-07-14 Miura Co Ltd Measuring method of water supply amount by means of water level in tank CN1791556A (en) * 2003-05-16 2006-06-21 æç¹éæ¯æ¬§æ´²å ¬å¸èé¨è¥¿ç»´å©å Method and device for treating water CN101403631A (en) * 2008-10-31 2009-04-08 æµæ±å¤§å¦ Liquid level on-line measurement method based on magnetic buoyancy WO2013073178A1 (en) * 2011-11-18 2013-05-23 æ ªå¼ä¼ç¤¾ æ±è Reactor water level measurement systemAddressee: Huang Dongsheng
Document name: the First Notification of an Office Action
2018-04-13 DD01 Delivery of document by public notice 2018-04-13 DD01 Delivery of document by public noticeAddressee: Huang Dongsheng
Document name: Notification of an Office Action
2018-10-30 GR01 Patent grant 2018-10-30 GR01 Patent grant 2020-01-17 TR01 Transfer of patent right 2020-01-17 TR01 Transfer of patent rightEffective date of registration: 20191230
Address after: Room 2, No.99, jimingtang South Road, Huaqiao Town, Kunshan, Suzhou City, Jiangsu Province
Patentee after: Kunshan long Zhaoyu Machinery Technology Co., Ltd
Address before: 110000, 3-4-3, No. two, 10-1 North Road, Dadong District, Liaoning, Shenyang
Patentee before: Huang Dongsheng
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