WO2021031775A1 - Implementation method for large book deacidification system - Google Patents
Implementation method for large book deacidification system Download PDFInfo
- Publication number
- WO2021031775A1 WO2021031775A1 PCT/CN2020/103479 CN2020103479W WO2021031775A1 WO 2021031775 A1 WO2021031775 A1 WO 2021031775A1 CN 2020103479 W CN2020103479 W CN 2020103479W WO 2021031775 A1 WO2021031775 A1 WO 2021031775A1
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- Prior art keywords
- deacidification
- liquid
- valve
- module
- air pressure
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- 238000000034 method Methods 0.000 title claims abstract description 49
- 239000007788 liquid Substances 0.000 claims abstract description 281
- 238000012545 processing Methods 0.000 claims abstract description 9
- 230000002159 abnormal effect Effects 0.000 claims abstract description 4
- 238000001514 detection method Methods 0.000 claims description 14
- 238000012423 maintenance Methods 0.000 claims description 11
- 238000010992 reflux Methods 0.000 claims description 8
- 238000012546 transfer Methods 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 4
- 238000007689 inspection Methods 0.000 claims 2
- 238000012360 testing method Methods 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 230000007547 defect Effects 0.000 abstract description 3
- 238000005259 measurement Methods 0.000 abstract 1
- 238000009833 condensation Methods 0.000 description 8
- 238000011084 recovery Methods 0.000 description 8
- 230000005494 condensation Effects 0.000 description 7
- 239000007921 spray Substances 0.000 description 5
- 239000000523 sample Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000013589 supplement Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000002572 peristaltic effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000013024 troubleshooting Methods 0.000 description 1
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Classifications
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/02—Chemical or biochemical treatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41M—PRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
- B41M7/00—After-treatment of prints, e.g. heating, irradiating, setting of the ink, protection of the printed stock
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/18—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00 of old paper as in books, documents, e.g. restoring
Definitions
- the patent of the invention relates to the technical field of deacidification protection of large books, in particular to the deacidification protection technology of paper cultural relics, archives, and books, and is specifically a method for realizing a large-scale book deacidification system.
- the existing large-scale book deacidification equipment is mainly liquid-phase equipment, which is mainly composed of liquid storage tanks, deacidification treatment tanks and corresponding liquid transmission pipelines and liquid circulation pipelines. Liquid immersion method, deacidification treatment. Further, in order to recover and reuse the deacidification liquid in the deacidification treatment tank, a condensation recovery device, an air pump and corresponding liquid recovery pipelines are added between the liquid storage tank and the deacidification treatment tank. In this way, the deacidification liquid gas dispersed in the paper deacidification equipment is collected, recovered by condensation, and finally returned to the liquid storage tank for further use.
- the above-mentioned deacidification treatment process and equipment lack a reasonable control method, which leads to the need for manual operation of the equipment, and the execution and conversion of each step are determined by the experience of the operator; any failure of the equipment is in use , All need to shut down for troubleshooting and repair, which reduces the efficiency of the equipment; the lack of real-time monitoring of equipment status and parameters in the equipment results in poor equipment safety.
- the above-mentioned defects limit the application of book deacidification equipment.
- this application provides a method for implementing a large-scale book deacidification system.
- the book deacidification method provided in this application has a short processing time, and can perform deacidification treatment on single pages, multiple pages and the entire book at the same time, with high efficiency.
- the implementation steps of the present invention are as follows:
- Step 1 First start the "pre-check module" to detect all the valves in the system equipment, the liquid level in the liquid storage tank 1, the concentration of the deacidified liquid in the deacidification treatment tank 2, and the air pressure in the liquid storage tank 1. a) If the test result is normal, go to step 2; b) If the test result is abnormal, go to step 3.
- Step 2 Execute the deacidification processing module.
- the drive motor 8 drives the book clamping device 7 to perform the deacidification treatment of books. After the deacidification treatment of the books is completed, step 4 is executed.
- Step 3 Start the emergency incident handling module:
- the working process of the emergency accident module is as follows. First, close the cover of the deacidification tank 2 and close all the valves in the equipment. Next, open the first one-way air valve 81 and the second one-way air valve 82, and turn on the air pump 10; after the air pump 10 runs for 5 minutes, the first air pressure sensor 71 located in the liquid storage tank 1 starts to detect the liquid storage tank 1.
- the air pressure judge whether the air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be stably maintained for more than 10 minutes in this state: a) If the liquid storage tank 1 cannot meet the above air pressure value requirements, then The system opens the eleventh valve 31 and the twelfth valve 32, and then the smart console prompts "equipment failure" on the display to wait for manual maintenance, and the alarm also alerts; b) If the liquid storage tank 1 meets the above-mentioned pressure value requirements , The second air pressure sensor 74 located in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2; judge whether the air pressure value is lower than 16kPa and can be maintained for more than 10 minutes: i) If yes, the system will shut down first All valves are then automatically shut down; ii) If not, the system opens the eleventh valve 31 and the twelfth valve 32, and then the smart console prompts "equipment failure"
- Step 4 Start the running detection module.
- the second air pressure sensor 74 in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2, and determines whether the measured air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2kPa, and can be stably maintained for more than 10 minutes in this state:
- step 5 If the air pressure value in the deacidification treatment tank 2 does not meet the conditions, perform step 5;
- the first air pressure sensor 71 in the liquid storage tank 1 starts to detect the air pressure in the liquid storage tank 1 and judges whether the measured pressure value is between 0.05 and 0.15 MPa If the value fluctuation range is less than 2kPa, and can be kept stable for more than 10 minutes in this state: i) If the air pressure value in the liquid storage tank 1 does not meet the conditions, perform step 5;
- Step 5 Execute the accident handling module.
- the accident handling module first start the liquid circulation module; then start the liquid return module, run for 10 minutes, and then judge the detection by the second buoy liquid level sensor 75 in the deacidification treatment tank 2
- the liquid level of the deacidified liquid a) If the detected liquid level is at "low level”, execute step 3 emergency accident module; b) if the liquid level is not "low level", then jump to the liquid in this step
- the reflow module continues to execute.
- Step 6 Execute the end operation module, and the system enters the end operation module", first execute the liquid circulation module, then start the liquid return module, and then judge whether the liquid level detected by the second buoy liquid level sensor 75 in the deacidification treatment tank 2 At the "low level”: a) If the level is not at the “low level”, skip to the "liquid reflux module” in this step and continue to reflux until the deacidification treatment tank 2 is at the "low level”; b) If the liquid level is at the "low liquid level", the system first closes all valves; then opens the second one-way valve 82, starts the suction pump 10, and after the suction pump 10 runs for 10 minutes, the second air pressure sensor in the deacidification treatment tank 2 74 Start to detect the air pressure in the deacidification treatment tank 2 to determine whether the air pressure value is lower than 16kPa and can be maintained for more than 10 minutes:
- the system closes the second one-way valve 82 and then opens the twelfth valve 32.
- the second air pressure sensor 74 in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2 , Determine whether the air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be kept stable for more than 10 minutes in this state: 1 If not, then the system opens the first valve (21) and the twelfth valve 32. Then the smart console prompts "equipment failure" on the display and waits for manual maintenance, and the alarm also alerts.
- the system opens the deacidification treatment tank 2, and then starts the eleventh valve 31. After waiting for 20 minutes of operation, the system closes all valves, and then the system automatically shuts down.
- step 1 pre-check module
- the first buoy liquid level sensor 72 in the first buoy starts to detect the liquid level in the liquid storage tank 1, and determines whether the detected liquid level is not lower than the "low liquid level”: i) If it is lower than the "low liquid level", the system Open the thirteenth valve 33, and then replenish the deacidified liquid to the liquid storage tank 1 through the liquid supplement pipe 99 until the liquid level is not lower than the "low liquid level”; ii) If it is not lower than the "low liquid level", then the liquid is stored
- the concentration sensor 73 in the tank 1 starts to detect the concentration in the liquid storage tank 1, and determines whether the sensor 73 detects that the concentration is not less than 1.5g/L: 1If it is less than 1.5g/L, then the automatic feeder 9 is turned on, and Add alkaline particles to the dea
- the specific work flow of the second deacidification treatment module is as follows: First, the system detects the height of the book through the first height sensor 76 and the second height sensor 77 to confirm whether the deacidification treatment tank 2 has been placed in the waiting process Books: a) If neither the first height sensor 76 nor the second height sensor 77 detects a book, the smart console will prompt "No book is inserted" through the display and the alarm will also give an alarm reminder;
- the required deacidification liquid level in the deacidification treatment tank 2 is the "medium level”; if the first height The sensor 76 and the second height sensor 77 both detect the book, and the required liquid level of the deacidification liquid in the deacidification treatment tank 2 is the "high level”;
- the system closes the deacidification treatment tank 2, and then starts the "liquid transmission module". After the "liquid transmission module” runs for 5 minutes, it determines the deacidification detected by the second buoy liquid level sensor 75 in the deacidification treatment tank 2. Whether the liquid level in the treatment tank 2 reaches the required liquid level: i) If it does not reach the required height, continue to execute the "liquid transfer module" until the required height is reached;
- the liquid circulation module is started, and then the driving motor 8 is started to make the book holding device 7 rotate and pull back and forth, and the running detection module is started synchronously.
- the working process of the liquid transfer module is as follows: the system first opens the first valve (21), then opens the second valve (22), then opens the first delivery device 3, and then opens the third valve (27).
- the working process of the liquid circulation module is as follows: the system first closes the second valve 22, then closes the third valve 27, and then sequentially opens the fourth valve 24, the second conveying device 4, the eighth valve 28, and the ninth valve 29, The fifth valve 25 and the tenth valve 30.
- the working process of the liquid return module is as follows: the system first closes the fourth valve 24, the eighth valve 28, the ninth valve 29, the fifth valve 25, and the tenth valve 30 in sequence, closes the second conveying device 4, and then opens in sequence The seventh valve 23, the first conveying device 3, and the sixth valve 26.
- the "low liquid level” means that the liquid level is about 5 mm higher than the bottom of the tank.
- the "high liquid level” is about 10 cm away from the top of the deacidification tank
- the "medium liquid level” means that the liquid level is about 60 cm higher than the bottom of the tank.
- the invention overcomes the defect that in the deacidification treatment process, there is a lack of a reasonable control method, manual operation is required, and the execution and conversion of each step are determined by the experience of the operator.
- Figure 1 The overall work flow chart of deacidification treatment system for books
- FIG. 11 Schematic diagram of the structure of the deacidification treatment system.
- 29-Ninth valve 30-Tenth valve; 31-Eleventh valve; 32-Twelfth valve;
- the deacidification treatment system for large quantities of paper includes:
- the bottom ends of the liquid storage tank 1 and the deacidification treatment tank 2 are placed on the same horizontal plane.
- the upper part of the liquid storage tank 1 and the deacidification treatment tank 2 are connected by a first gas pipeline 91, and the pipeline is provided with a first valve 21.
- An upper part of the other side of the liquid storage tank 1 is provided with a liquid supplement pipe 99, and the thirteenth valve 33 is arranged on the liquid supplement pipe 99.
- the bottom of the liquid storage tank 1 and the deacidification treatment tank 2 are connected by a first liquid pipeline 92, the first conveying device 3 is arranged in the first liquid pipeline 92, and the second valve 22 and the third valve 27 are both arranged in the first liquid pipeline 92.
- a liquid pipeline 92 is located on both sides of the first conveying device 3.
- the pipeline leading from the bottom of the liquid storage tank 1 is connected with a second three-way pipe 52, and a sixth three-way pipe 56 and an eighth third are respectively provided on both sides of the first conveying device 3.
- a second three-way pipe 52 the pipeline leading from the bottom of the penetration deacidification tank 2 is connected with a 53 third three-way pipe, which is connected with the third valve 27.
- the first liquid pipeline 92 (from the liquid storage tank to the deacidification treatment tank) is sequentially connected with: the second three-way pipe 52, the second valve 22, the sixth three-way pipe 56, the first conveying device 3, and the eighth The three-way pipe 58, the third valve 27, and the third three-way pipe 53.
- the second liquid pipeline 94 and the first liquid pipeline 92 share a pipeline section that penetrates into the liquid storage tank 1 and a pipeline section that penetrates into the deacidification treatment tank 2.
- the second liquid pipeline 94 (from the liquid storage tank to The direction of the deacidification tank) are connected in sequence: the sixth valve 26, the eighth three-way pipe 58, the first conveying device 3, the sixth three-way pipe 56, the seventh valve 23, the first three-way pipe 51, and the third Three-way pipe 53.
- One side of the deacidification treatment tank 2 is equipped with a first liquid circulation pipe 93; a second liquid circulation pipe 95; on the other side, a third liquid circulation pipe 96 and a fourth liquid circulation pipe 97 are respectively installed:
- One end of the first liquid circulation pipeline 93 is connected with the first three-way pipe 51 and the other end is inserted into the deacidification treatment tank 2 away from the bottom end of the deacidification treatment tank 2, and the pipe port is provided with a spray device.
- the first liquid circulation pipeline 93 is provided with a fourth valve 24 and a second conveying device 4; the fourth valve 24 is connected to the first three-way pipe 51, and the second conveying device 4 is connected to the fourth valve 24.
- the second liquid circulation pipeline 95 and the first liquid circulation pipeline 93 are connected by a fourth three-way pipe 54.
- the second liquid circulation pipeline 95 is inserted into the deacidification treatment tank at the bottom end away from the deacidification treatment tank 2.
- An injection device is provided on the pipeline port, and an eighth valve 28 is installed on the second liquid circulation pipeline 95 between the fourth three-way pipe 54 and the injection device of the second liquid circulation pipeline 95.
- a fifth valve 25 is installed on the first liquid circulation pipe 93 between the fourth three-way pipe 54 and the spray device of the first liquid circulation pipe 93.
- the third liquid circulation pipeline 96 is connected to the first liquid circulation pipeline 93 through a seventh three-way pipe 57.
- the fourth liquid circulation pipeline 97 is connected to the third liquid circulation pipeline 96 through the fifth three-way pipe 55.
- the third liquid circulation pipe 96 and the fourth liquid circulation pipe 97 are respectively inserted into the deacidification treatment tank 2 at the bottom end away from the deacidification treatment tank 2, and the pipe ports are equipped with spray devices.
- the third liquid circulation pipe 96 A ninth valve 29 and a tenth valve 30 are installed between the fifth three-way pipe 55 and the spray device with the fourth liquid circulation pipeline 97, respectively.
- the first conveying device 3 and the second conveying device 4 may be either a centrifugal pump that can only be forwardly conveyed, or a peristaltic pump that can be conveyed in both forward and reverse directions.
- the inner wall of the deacidification tank 2 is provided with a first height detector 76 and a second height detector 77.
- the height of the first height detector 76 is higher than the height of the book holding device 7 by about 5 cm, and the second height detector 77 It is about 15 cm higher than the first height detector 76.
- the top of the liquid storage tank 1 is provided with a cover.
- One end of the first gas condensing pipe 83 passes through the cover and a first air pressure sensor 71 is provided at the port position, and the other end is connected to the condensate collector 11, and the first gas condensing pipe 83 is
- a first one-way air valve 81 is provided, and a first air pressure sensor 71 is suspended above the liquid surface of the liquid storage tank 1 for measuring the internal air pressure of the liquid storage tank 1.
- One end of the condensed liquid return line 85 is connected to the condensate recovery device 11, and the other end passes through the cover of the liquid storage tank 1 and is inserted into the tank.
- the condensed liquid return line 85 is provided with an eleventh valve 31.
- One end of the first buoy liquid level sensor 72 and the concentration sensor 73 pass through the cover of the liquid storage tank 1, and the probe is placed in the tank, and the other end is located outside the cover of the liquid storage tank 1.
- the probe position of the concentration sensor 73 is slightly higher At the bottom of the liquid storage tank 1.
- the automatic feeder 9 is arranged on the cover of the liquid storage tank 1, and its conveying pipeline passes through the cover of the liquid storage tank 1, and is inserted into the tank for feeding alkaline particles.
- a stirring device 16 is provided in the liquid storage tank 1 to prevent precipitation of the liquid due to long-term storage.
- a cover is provided on the top of the deacidification treatment tank 2, and one end of the second buoy liquid level sensor 75 and the second gas pipeline 98 passes through the cover of the deacidification treatment tank 2, and the probe of the second buoy liquid level sensor 75 is located in the deacidification treatment tank 2.
- a twelfth valve 32 is provided inside the processing tank 2 inside the processing tank 2 inside the processing tank 2 inside the processing tank 2 inside the processing tank 2; a twelfth valve 32 is provided on the pipeline outside the cover of the second gas pipeline 98.
- the connecting part of the book holding device 7 passes through the cover of the deacidification tank 2 and is connected to the rotating shaft of the driving motor 8 on the cover.
- the upper end of the connecting part of the drive motor 8 and the book holding device 7 in the deacidification tank 2 is equipped with a second air pressure sensor 74, which is suspended above the liquid level of the deacidification tank 2 for Measure the internal air pressure of the deacidification treatment tank 2; one end of the second gas condensing pipe 84 passes through the cover of the deacidification treatment tank 2, and the other end is connected with the air pump 10, and the second gas condensing pipe 84 is provided with a first Two one-way air valves 82; the air pump 10 is connected to the condensate recovery device 11 through a pipeline.
- the first conveying device 3 and the second conveying device 4 are centrifugal pumps that can only transmit forward, or peristaltic pumps that can transmit both forward and reverse.
- the spraying device is a spray gun or a nozzle.
- the driving motor 8 is a stepping motor or a servo motor.
- All valves, the first one-way air valve 81, the second one-way air valve 82, the first conveying device 3, the second conveying device 4, the suction pump 10, the condensation recovery device 11, the automatic feeder 9, the drive motor 8, all Both the sensor and the height detector are connected to and controlled by the smart console.
- All valves refer to: first valve 21; second valve 22; third valve 27; fourth valve 24; fifth valve 25; sixth valve 26; seventh valve 23; eighth valve 28; ninth valve 29 ;
- All sensors and height detectors refer to: the first air pressure sensor 71; the first buoy liquid level sensor 72; the concentration sensor 73; the second air pressure sensor 74; the second buoy liquid level sensor 75;
- Step 1 First start the pre-check module to detect all the valves in the system equipment, the liquid level in the liquid storage tank 1, the concentration of the deacidification liquid in the deacidification treatment tank 2, and the air pressure in the liquid storage tank 1, a) If the detection result is normal, go to step 2; b) If the detection result is abnormal, go to step 3.
- the working process of the pre-check module is as follows: check whether all valves in the system equipment are in a closed state: c) If not, the system will close all valves;
- the first buoy liquid level sensor 72 in the liquid storage tank 1 starts to detect the liquid level in the liquid storage tank 1, and determines whether the detected liquid level is not lower than the "low liquid level” (low liquid level) It means that the liquid level is about 5mm higher than the bottom of the tank): i) If it is lower than the "low liquid level", the system opens the thirteenth valve 33, and then through the replenishment pipeline 99, the liquid storage tank 1 is refilled with deacidified liquid until the liquid Level is not lower than the "low level”; ii) if it is not lower than the "low level”, the concentration sensor 73 in the liquid storage tank 1 starts to detect the concentration in the liquid storage tank 1, and determines whether the sensor 73 detects the concentration Not less than 1.5g/L: 1If it is less than 1.5g/L, the automatic feeder 9 is turned on, and the alkaline substance particles are added to the deacidified liquid in the storage tank 1 until the concentration is not less than 1.5g/L L; 2If the concentration is not less than 1.5g
- Step 2 Execute the deacidification processing module.
- the drive motor 8 drives the book clamping device 7 to perform the deacidification processing of the books.
- execute step 4 to start the running detection module.
- the work flow of the deacidification treatment module is as follows: First, the system detects the height of the book through the first height sensor 76 and the second height sensor 77 to confirm whether the book to be processed has been placed in the deacidification treatment tank 2 : A) If neither the first height sensor 76 nor the second height sensor 77 detects a book, the smart console will prompt "No book is inserted" through the display and the alarm will also give an alarm reminder;
- the required deacidification liquid level in the deacidification treatment tank 2 is "medium level” (medium level refers to The liquid level is about 60cm higher than the bottom of the tank); if both the first height sensor 76 and the second height sensor 77 detect books, the required liquid level of the deacidification liquid in the deacidification treatment tank 2 is "high level” ( Refers to the liquid level is 10cm from the top of the deacidification tank).
- the system closes the deacidification treatment tank 2, and then starts the "liquid transmission module". After the "liquid transmission module” runs for 5 minutes, it determines the deacidification detected by the second buoy liquid level sensor 75 in the deacidification treatment tank 2. Whether the liquid level in the treatment tank 2 reaches the required liquid level: i) If it does not reach the required height, continue to execute the "liquid transfer module" until the required height is reached;
- Step 3 Start the emergency incident handling module.
- the working process of the emergency accident module is as follows. First, close the cover of the deacidification tank 2 and close all the valves in the equipment. Next, open the first one-way air valve 81 and the second one-way air valve 82, and turn on the air pump 10; after the air pump 10 runs for 5 minutes, the first air pressure sensor 71 located in the liquid storage tank 1 starts to detect the liquid storage tank 1.
- the air pressure judge whether the air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be stably maintained for more than 10 minutes in this state: a) If the liquid storage tank 1 cannot meet the above air pressure value requirements, then The system opens the eleventh valve 31 and the twelfth valve 32, and then the smart console prompts "equipment failure" on the display to wait for manual maintenance, and the alarm also alerts; b) If the liquid storage tank 1 meets the above-mentioned pressure value requirements , The second air pressure sensor 74 located in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2; judge whether the air pressure value is lower than 16kPa and can be maintained for more than 10 minutes: i) If yes, the system will shut down first All valves are then automatically shut down; ii) If not, the system opens the eleventh valve 31 and the twelfth valve 32, and then the smart console prompts "equipment failure"
- Step 4 Start the running detection module.
- the second air pressure sensor 74 in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2, and determines whether the measured air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2kPa, and can be kept stable for more than 10min in this state:
- step 5 identity handling module
- step 5 If the air pressure value in the deacidification treatment tank 2 satisfies the conditions, the first air pressure sensor 71 in the liquid storage tank 1 starts to detect the air pressure in the liquid storage tank 1 and judges whether the measured pressure value is between 0.05 and 0.15 MPa The value fluctuation range is less than 2kPa, and can be kept stable for more than 10min in this state: i) If the air pressure value in the liquid storage tank 1 does not meet the conditions, perform step 5 (accident handling module);
- step 6 If the air pressure value in the liquid storage tank 1 satisfies the conditions, finally judge whether the book deacidification process has been running for 1h; 1If the above process has lasted for 1h, then perform step 6 to end the running module; 2If the above process does not It lasts for 1 hour and jumps to the beginning of this step (that is, in step 4, the second air pressure sensor 74 in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2) to continue execution.
- Step 5 Execute the accident handling module.
- the accident handling module first start the “liquid circulation module” and then start the “liquid return module”. After running for 10 minutes, determine the second buoy level sensor in the deacidification tank 2 75 The liquid level of the deacidified liquid detected: a) If the detected liquid level is at "low level”, execute step 3 emergency accident module; b) if the liquid level is not "low level”, then jump to The liquid reflux module of this step continues to execute.
- Step 6 Execute the end operation module.
- the system After the system enters the "end operation module”, first execute the liquid circulation module, then start the liquid return module, and then determine the liquid detected by the second buoy liquid level sensor 75 in the deacidification treatment tank 2. Whether the liquid level is at the "low level”: a) If the liquid level is not at the “low level”, skip to the liquid reflux module in this step and reflow until the deacidification treatment tank 2 is at the "low level”; b) if When the liquid level is at the "low liquid level”, the system first closes all valves; then opens the second one-way valve 82, starts the suction pump 10, and after the suction pump 10 runs for 10 minutes, the second air pressure sensor 74 in the deacidification treatment tank 2 Start to detect the air pressure in the deacidification tank 2 to determine whether the air pressure value is lower than 16kPa and can be maintained for more than 10 minutes:
- the system closes the second one-way valve 82 and then opens the twelfth valve 32.
- the second air pressure sensor 74 in the deacidification treatment tank 2 starts to detect the air pressure in the deacidification treatment tank 2 , Determine whether the air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be kept stable for more than 10 minutes in this state: 1 If not, then the system opens the first valve 21 and the twelfth valve 32, Then the smart console prompts "equipment failure" through the display to wait for manual maintenance, and the alarm also alerts.
- the system opens the deacidification treatment tank 2, and then starts the eleventh valve 31, and waits for 20 minutes after running (the purpose is to wait for the condensation recovery device 11 to work for 20 minutes to condense the gas collected in the deacidification treatment tank 2 After it becomes liquid, it returns to the liquid storage tank 1), the system closes all valves, and then the system automatically shuts down.
- liquid transfer module The working procedures of the liquid transfer module, liquid circulation module, and liquid return module are respectively introduced as follows:
- the system first opens the first valve 21, then opens the second valve 22, then opens the first conveying device 3, and then opens the third valve 27.
- the system closes the second valve 22 first, then closes the third valve 27, and then opens the fourth valve 24, the second conveying device 4, the eighth valve 28, the ninth valve 29, the fifth valve 25, and the tenth valve 30 in sequence.
- the system first closes the fourth valve 24, the eighth valve 28, the ninth valve 29, the fifth valve 25, and the tenth valve 30 in sequence, closes the second conveying device 4, and then sequentially opens the seventh valve 23, the first conveying device 3, The sixth valve 26.
Abstract
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Claims (9)
- 一种大型图书脱酸系统的实现方法,其特征在于:智能控制台开启后,冷凝回收器(11)启动,待5min的预热时间结束,设备正常启动后,脱酸处理的工作流程具体如下:A method for implementing a large-scale book deacidification system, which is characterized in that: after the smart console is turned on, the condensate collector (11) is started, and after the preheating time of 5 minutes is over, after the equipment is started normally, the work flow of deacidification is as follows :步骤一、首先启动“预检模块”,将系统设备中所有阀门、储液罐(1)中的液位、脱酸处理罐(2)中的脱酸液浓度以及储液罐(1)中的气压的进行检测,a)若检测结果为正常,执行步骤二;b)若检测结果为不正常,执行步骤三;Step 1. Start the "pre-check module" first, and set all valves in the system equipment, the liquid level in the liquid storage tank (1), the concentration of the deacidified liquid in the deacidification treatment tank (2), and the liquid storage tank (1) If the detection result is normal, perform step 2; b) if the detection result is abnormal, perform step 3;步骤二、执行脱酸处理模块,本步骤中进行驱动电机(8)带动书籍夹持装置(7)进行书籍的脱酸处理,待书籍脱酸处理结束后,执行步骤四;Step 2: Execute the deacidification processing module. In this step, the drive motor (8) drives the book holding device (7) to perform the deacidification treatment of the books. After the deacidification treatment of the books is completed, perform step 4;步骤三、启动应急事故处理模块:Step 3: Start the emergency incident handling module:应急事故模块的工作流程如下,首先依次关闭脱酸处理罐(2)盖体,关闭设备中所有的阀门;其次开启第一单向气阀(81)和第二单向气阀(82),以及开启抽气泵(10);待抽气泵(10)运行5min后,位于储液罐(1)中的第一气压传感器(71)开始检测储液罐(1)中的气压,判断气压数值是否位于0.05~0.15MPa之间、并且数值波动范围小于2kPa、并且能在这个状态下稳定保持10min以上:a)如果储液罐(1)无法满足上述的气压数值要求,则系统开启第十一阀门(31)和第十二阀门(32),然后智能控制台通过显示器提示“设备故障”等待人工检修,同时报警器也进行报警提醒;b)如果储液罐(1)满足上述的气压数值要求,则位于脱酸处理罐(2)中的第二气压传感器(74)开始检测脱酸处理罐(2)中的气压;判断气压数值是否低于16kPa,并能保持10min以上:i)如果是,则系统会先关闭所有的阀门,然后自动关机;ii)如果不是,则系统开启第十一阀门(31)和第十二阀门(32),然后智能控制台通过显示器提示“设备故障”等待人工检修,同时报警器也进行报警提醒;The working process of the emergency accident module is as follows. First, close the cover of the deacidification tank (2) and close all the valves in the equipment; then open the first one-way valve (81) and the second one-way valve (82), And turn on the air pump (10); after the air pump (10) runs for 5 minutes, the first air pressure sensor (71) located in the liquid storage tank (1) starts to detect the air pressure in the liquid storage tank (1) to determine whether the air pressure value is Located between 0.05~0.15MPa, and the value fluctuation range is less than 2kPa, and can be kept stable for more than 10 minutes in this state: a) If the liquid storage tank (1) cannot meet the above-mentioned pressure value requirements, the system opens the eleventh valve (31) and the twelfth valve (32), then the intelligent console will prompt "equipment failure" through the display to wait for manual maintenance, and the alarm will also give an alarm reminder; b) If the liquid storage tank (1) meets the above-mentioned pressure value requirements , The second air pressure sensor (74) located in the deacidification treatment tank (2) starts to detect the air pressure in the deacidification treatment tank (2); judge whether the air pressure value is lower than 16kPa and can be maintained for more than 10 minutes: i) If yes , The system will close all valves first, and then automatically shut down; ii) If not, the system will open the eleventh valve (31) and the twelfth valve (32), and then the smart console will prompt "equipment failure" on the display and wait Manual inspection and repair, and the alarm will also alert;步骤四、启动运行中检测模块,在该模块中,首先脱酸处理罐(2)中第二气压传感器(74)开始检测脱酸处理罐(2)中的气压,并判断所测得的气压数值是否在0.05~0.15MPa之间、并且数值波动范围小于2kPa、并且能在这个状态下稳定保持10min以上:Step 4. Start the running detection module. In this module, the second air pressure sensor (74) in the deacidification treatment tank (2) starts to detect the air pressure in the deacidification treatment tank (2) and judges the measured air pressure Whether the value is between 0.05 and 0.15 MPa, and the fluctuation range of the value is less than 2 kPa, and can be kept stable for more than 10 minutes in this state:a)如果脱酸处理罐(2)中气压值不满足条件,则执行步骤五;a) If the air pressure value in the deacidification tank (2) does not meet the conditions, perform step 5;b)如果脱酸处理罐(2)中气压值满足条件,其次储液罐(1)中的第一气压传感器(71)开始检测储液罐(1)中的气压,并判断所测得的气压数值是否在0.05~0.15MPa之间、并且数值波动范围小于2kPa、并且能在这个状态下稳定保持10min以上:b) If the air pressure value in the deacidification tank (2) meets the conditions, the first air pressure sensor (71) in the liquid storage tank (1) starts to detect the air pressure in the liquid storage tank (1) and judges the measured pressure Whether the air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be kept stable for more than 10 minutes in this state:i)如果储液罐(1)中的气压值不满足条件,则执行步骤五;i) If the air pressure value in the liquid storage tank (1) does not meet the conditions, go to step 5;ii)如果储液罐(1)中的气压值满足条件,最后判断书籍脱酸处理过程是否已运行了1h;①如果上述过程已经持续1h,那么执行步骤六结束运行模块;②如果上述过程没有持续1h,跳转到本步骤的开始继续执行;ii) If the air pressure value in the liquid storage tank (1) meets the conditions, finally judge whether the book deacidification process has been running for 1h; ①If the above process has lasted for 1h, then perform step 6 to end the running module; ②If the above process has not Continue for 1h, jump to the beginning of this step to continue execution;步骤五、执行事故处理模块,在事故处理模块中,首先启动液体循环模块;再启动液体回流模块,运行10min后,然后判断位于脱酸处理罐(2)中的第二浮标液位传感器(75)检测到的脱酸液的液位:a)如果检测到的液位处于“低液位”,则执行步骤三应急事故模块;b)如果液位不是“低液位”,则跳转到本步骤的液体回流模块继续执行;Step 5. Execute the accident handling module. In the accident handling module, first start the liquid circulation module; then start the liquid return module, run for 10 minutes, and then judge the second buoy level sensor (75) located in the deacidification treatment tank (2) ) The liquid level of the deacidified liquid detected: a) If the detected liquid level is at the "low level", execute step 3 emergency accident module; b) If the liquid level is not "low level", jump to The liquid reflux module of this step continues to execute;步骤六、执行结束运行模块,系统进入结束运行模块”,首先执行液体循环模块,再启动液体回流模块,然后判断脱酸处理罐(2)中的第二浮标液位传感器(75)所检测到的液位是否处于“低液位”:a)如果液位不处于“低液位”,跳转到本步骤中的“液体回流模块”继续进行回流直到脱酸处理罐(2)处于“低液位”;b)如果液位处于“低液位”,则系统首先关闭所有的阀门;然后开启第二单向阀(82),启动抽气泵(10),抽气泵(10)运行10min后,脱酸处理罐(2)中的第二气压传感器(74)开始检测脱酸处理罐(2)中的气压,判断气压数值是否低于16kPa、并且能保持10min以上:Step 6. Execute the end operation module, and the system enters the end operation module", first execute the liquid circulation module, then start the liquid return module, and then judge the detection by the second buoy liquid level sensor (75) in the deacidification treatment tank (2) Is the liquid level at the "low level": a) If the liquid level is not at the "low level", skip to the "liquid reflux module" in this step and continue to reflux until the deacidification tank (2) is at "low" Liquid level"; b) If the liquid level is at "low liquid level", the system first closes all valves; then opens the second check valve (82), starts the air pump (10), and the air pump (10) runs for 10 minutes , The second air pressure sensor (74) in the deacidification treatment tank (2) starts to detect the air pressure in the deacidification treatment tank (2) to determine whether the air pressure value is lower than 16kPa and can be maintained for more than 10 minutes:i)如果不是,那么则系统开启第一阀门(21)和第十二阀门(32),然后智能控制台通过显示器提示“设备故障”等待人工检修,同时报警器也进行报警提醒;i) If it is not, then the system opens the first valve (21) and the twelfth valve (32), and then the intelligent console prompts "equipment failure" through the display to wait for manual maintenance, and the alarm also alerts;ii)如果是,那么系统关闭第二单向阀(82),然后开启第十二阀门(32),运行10min后,位于脱酸处理罐(2)中的第二气压传感器(74)开始检测脱酸处理罐(2)中的气压,判断气压数值是否位于0.05~0.15MPa之间、并且数值波动范围小于2kPa、并且能在这个状态下稳定保持10min以上:①如果不是,那么则系统开启第一阀门(21)和第十二阀门(32),然后智能控制台通过显示器提示“设备故障”等待人工检修,同时报警器也进行报警提醒;ii) If yes, the system closes the second one-way valve (82), and then opens the twelfth valve (32). After running for 10 minutes, the second air pressure sensor (74) in the deacidification tank (2) starts to detect For the air pressure in the deacidification tank (2), judge whether the air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be kept stable for more than 10 minutes in this state: ① If not, then the system is turned on One valve (21) and the twelfth valve (32), and then the intelligent console prompts "equipment failure" through the display to wait for manual maintenance, and the alarm also alerts;②如果是,则系统打开脱酸处理罐(2),然后启动第十一阀门(31),等待运行20min后,系统关闭所有阀门,然后系统自动关机。②If it is, the system opens the deacidification tank (2), and then starts the eleventh valve (31). After waiting for 20 minutes, the system closes all valves, and then the system automatically shuts down.
- 根据权利要求1所述的一种大型图书脱酸系统的实现方法,其特征在于:步骤 一“预检模块”的具体工作流程如下:检测系统设备中的所有阀门是否处于关闭的状态:c)如果不是,系统将关闭所有阀门;d)如果是,则储液罐(1)中的第一浮标液位传感器(72)开始检测储液罐(1)中的液位,并判断检测到的液位是否不低于“低液位”:i)如果低于“低液位”,则系统开启第十三阀门(33),然后通过补液管路(99),对储液罐(1)补充脱酸液直到液位不低于“低液位”;ii)如果不低于“低液位”,则储液罐(1)中的浓度传感器(73)开始检测储液罐(1)中的浓度,并判断传感器(73)检测到浓度是否不低于1.5g/L:①如果低于1.5g/L,那么自动投料机(9)开启,并向储液罐(1)中的脱酸液中加入碱性物质颗粒,直到浓度不低于1.5g/L;②如果浓度不低于1.5g/L,则位于储液罐(1)中的第一气压传感器(71)开始检测储液罐(1)中的气压,并判断所检测到的气压数值是否位于0.05~0.15MPa之间、并且数值波动范围小于2kPa、并且能在这个状态下稳定保持10min以上:The method for implementing a large-scale book deacidification system according to claim 1, characterized in that: the specific workflow of the "pre-inspection module" in step one is as follows: detecting whether all valves in the system equipment are in a closed state: c) If not, the system will close all valves; d) If yes, the first buoy liquid level sensor (72) in the liquid storage tank (1) starts to detect the liquid level in the liquid storage tank (1) and judges the detected Whether the liquid level is not lower than the "low liquid level": i) If it is lower than the "low liquid level", the system opens the thirteenth valve (33), and then through the replenishing pipeline (99), to the liquid tank (1) Replenish deacidified liquid until the liquid level is not lower than the "low liquid level"; ii) If it is not lower than the "low liquid level", the concentration sensor (73) in the liquid storage tank (1) starts to detect the liquid storage tank (1) And determine whether the concentration detected by the sensor (73) is not less than 1.5g/L: ①If it is less than 1.5g/L, then the automatic feeder (9) will be turned on and send to the liquid storage tank (1) Add alkaline particles to the deacidification solution until the concentration is not less than 1.5g/L; ②If the concentration is not less than 1.5g/L, the first air pressure sensor (71) located in the liquid storage tank (1) starts to detect The air pressure in the liquid storage tank (1), and determine whether the detected air pressure value is between 0.05 and 0.15 MPa, and the value fluctuation range is less than 2 kPa, and can be stably maintained for more than 10 minutes in this state:α)如果是,则系统进入“脱酸处理模块”;α) If yes, the system enters the "deacidification module";β)如果无法实现上述的气压数值要求,则系统进入“应急事故模块”。β) If the above air pressure value requirements cannot be achieved, the system enters the "emergency accident module".
- 根据权利要求1所述的一种大型图书脱酸系统的实现方法,其特征在于:步骤二脱酸处理模块具体的工作流程如下:首先,系统通过第一高度传感器(76)和第二高度传感器(77)来检测书籍的高度,以确认脱酸处理罐(2)中是否已放入待处理的书籍:The method for implementing a large-scale book deacidification system according to claim 1, characterized in that: the specific work flow of the second deacidification processing module is as follows: first, the system passes through the first height sensor (76) and the second height sensor (77) To detect the height of the book to confirm whether the book to be processed has been placed in the deacidification tank (2):a)如果第一高度传感器(76)和第二高度传感器(77)均未检测到书籍,则智能控制台通过显示器提示“未放入书籍”同时报警器也进行报警提醒;a) If neither the first height sensor (76) nor the second height sensor (77) detects the book, the smart console will prompt "No book is inserted" through the display and the alarm will also give an alarm reminder;b)如果第一高度传感器(76)检测到书籍,而第二高度传感器(77)未检测到书籍,则脱酸处理罐(2)中所需脱酸液的液位高度为“中液位”;如果第一高度传感器(76)和第二高度传感器(77)均检测到书籍,则脱酸处理罐(2)中所需脱酸液的液位高度为“高液位”;b) If the first height sensor (76) detects a book, but the second height sensor (77) does not detect a book, the required deacidification liquid level in the deacidification treatment tank (2) is "medium level" "; if the first height sensor (76) and the second height sensor (77) both detect books, the required deacidification liquid level in the deacidification treatment tank (2) is "high level";然后,系统关闭脱酸处理罐(2),随后启动“液体传输模块”,待“液体传输模块”运行5min后,判断位于脱酸处理罐(2)中的第二浮标液位传感器(75)所检测到的脱酸处理罐(2)中的液位是否达到所需的液位高度:i)如果没达到所需高度的液位,继续执行“液体传输模块”,直到达到所需高度液位;Then, the system closes the deacidification treatment tank (2), and then starts the "liquid transmission module". After the "liquid transmission module" runs for 5 minutes, it is judged that the second float level sensor (75) located in the deacidification treatment tank (2) Whether the detected liquid level in the deacidification treatment tank (2) reaches the required liquid level: i) If the liquid level does not reach the required height, continue to execute the "liquid transfer module" until the required height is reached. Bitii)如果达到所需高度的液位,则启动液体循环模块,然后启动驱动电机(8)使得书籍加持装置(7)做旋转提拉往复运动,并同步启动运行中检测模块。ii) If the liquid level of the required height is reached, start the liquid circulation module, and then start the drive motor (8) to make the book holding device (7) rotate and pull back and forth, and start the running detection module synchronously.
- 根据权利要求3所述的一种大型图书脱酸系统的实现方法,其特征在于:液体传输模块的工作流程如下:The method for implementing a large-scale book deacidification system according to claim 3, wherein the working process of the liquid transfer module is as follows:系统先开启第一阀门(21),再开启第二阀门(22),然后开启第一输送装置(3),然后开启第三阀门(27)。The system first opens the first valve (21), then opens the second valve (22), then opens the first delivery device (3), and then opens the third valve (27).
- 根据权利要求1或3所述的一种大型图书脱酸系统的实现方法,其特征在于:液体循环模块的工作流程如下:The method for implementing a large-scale book deacidification system according to claim 1 or 3, wherein the working process of the liquid circulation module is as follows:系统先关闭第二阀门(22),再关闭第三阀门(27),然后依次开启第四阀门(24),第二输送装置(4),第八阀门(28),第九阀门(29),第五阀门(25),第十阀门(30)。The system first closes the second valve (22), then closes the third valve (27), then sequentially opens the fourth valve (24), the second conveying device (4), the eighth valve (28), and the ninth valve (29) , The fifth valve (25), the tenth valve (30).
- 根据权利要求1所述的一种大型图书脱酸系统的实现方法,其特征在于:液体回流模块的工作流程如下:The method for implementing a large-scale book deacidification system according to claim 1, wherein the working process of the liquid recirculation module is as follows:系统先依次关闭第四阀门(24)、第八阀门(28)、第九阀门(29)、第五阀门(25)、第十阀门(30)、第二输送装置(4),然后依次开启第七阀门(23)、第一输送装置(3)、第六阀门(26)。The system first closes the fourth valve (24), the eighth valve (28), the ninth valve (29), the fifth valve (25), the tenth valve (30), and the second conveying device (4) in sequence, and then opens in sequence The seventh valve (23), the first delivery device (3), and the sixth valve (26).
- 根据权利要求1或2所述的一种大型图书脱酸系统的实现方法,其特征在于:所述“低液位”是指液位高于罐底5mm左右。The method for implementing a deacidification system for large books according to claim 1 or 2, characterized in that: the "low liquid level" means that the liquid level is about 5 mm higher than the bottom of the tank.
- 根据权利要求3所述的一种大型图书脱酸系统的实现方法,其特征在于:所述“高液位”距离脱酸处理罐顶部10cm左右。The method for implementing a deacidification system for large books according to claim 3, wherein the "high liquid level" is about 10 cm away from the top of the deacidification tank.
- 根据权利要求3所述的一种大型图书脱酸系统的实现方法,其特征在于:所述“中液位”指液位高于罐底60cm左右。The method for implementing a deacidification system for large books according to claim 3, characterized in that: the "medium liquid level" means that the liquid level is about 60 cm higher than the bottom of the tank.
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CN112391872A (en) | 2021-02-23 |
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