CN212640033U - Membrane system for cleaning fluid regeneration of dairy - Google Patents
Membrane system for cleaning fluid regeneration of dairy Download PDFInfo
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- CN212640033U CN212640033U CN202021000792.XU CN202021000792U CN212640033U CN 212640033 U CN212640033 U CN 212640033U CN 202021000792 U CN202021000792 U CN 202021000792U CN 212640033 U CN212640033 U CN 212640033U
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Abstract
A ceramic membrane system for cleaning solution regeneration of a dairy plant comprises ceramic membrane filtering equipment, a raw liquid tank and a clear liquid tank. Feeding the raw liquid tank to a ceramic membrane device, concentrating turbid cleaning liquid by the ceramic membrane device, and filtering clear cleaning liquid; the concentrated solution returns to the stock solution tank to continue circulation, and the clarified filtrate is collected in a clear solution tank. The ceramic membrane filtering equipment can be produced by using an automatic program and continuously operates for 8-10 hours, so that the risk caused by manual operation is avoided. The whole set of equipment comprises a membrane component, a circulating pump, a circulating loop, a balance cylinder system, a flow regulating unit, a temperature control unit, a cleaning unit and the like. The ceramic membrane component adopts a gradient ceramic membrane, can form time-stable production flux, has the service temperature of 90 ℃ at most and the aperture of 20-50 nanometers, and meets the working condition of clarifying and recycling the used cleaning solution. Meanwhile, the ceramic membrane component can be cleaned in a backwashing mode. And the automatic cleaning agent adding unit is used for realizing automatic addition of the cleaning agent and execution of the cleaning step through a program. And the regulating system is provided with concentrated solution and clarified solution, the concentration times of operation are set according to the flow rates of the concentrated solution and the clarified solution, and the recovery rate of the cleaning solution is more than 85 percent according to the accumulation amount of the clarified solution.
Description
Technical Field
The utility model relates to a washing liquid clarification filtration equipment, especially a membrane filtration system that is used for the acid-base washing liquid clarification regeneration of dairy products beverage factory.
Background
The cleaning liquid of the dairy beverage factory can dissolve a large amount of organic matters such as protein, fat and the like after being used for a period of time, the impurity content of the cleaning liquid is increased, the cleaning effect on production equipment is reduced, longer cleaning time and higher cleaning temperature are needed, and the energy consumption in the cleaning process of the equipment is increased; meanwhile, impurities in the cleaning solution are easy to deposit and attach in the dilute acid and dilute alkali tanks, and the dilute acid and dilute alkali tanks need to be cleaned more and more frequently. The traditional method is to discharge settled impurities from the bottom of the tank and reuse the supernatant, and the cleaning liquid obtained by the method is not clean and the cleaning effect is not improved. The use period is shortened, the cleaning agent is discharged periodically, and a new acid-base cleaning solution is prepared, so that the cleaning effect can be recovered. But the discharge of waste acid and alkali liquor is increased, the amount of wastewater in a factory is increased, and the cost of sewage treatment is correspondingly increased. The new preparation of the acid-base cleaning solution also increases the operation cost of factories such as concentrated acid-base purchase cost, water consumption, steam consumption and the like.
The most protein in milk is 10-1000 nm, while the fat is 1-10 microns. Membrane filtration is a separation process that relies on differences in molecular or particle size and has very wide application in the dairy and beverage industries. The ceramic membrane of 20-50 nanometers is selected, most of protein and fat can be intercepted, and acid-base cleaning solution is regenerated to the maximum extent. Meanwhile, the acid-base temperature and the pH value after use are high, and the ceramic membrane material can bear high temperature and extreme pH (0-14), so that the method is more suitable for the application scene.
Disclosure of Invention
An object of the utility model is to provide a ceramic membrane system for cleaning solution regeneration of dairy plant solves above at least one technical problem.
The technical solution of the utility model is as follows:
a ceramic membrane system for regenerating a cleaning solution in a dairy plant comprises ceramic membrane filtering equipment, a stock solution tank and a cleaning solution tank, and is characterized in that the ceramic membrane filtering equipment comprises a membrane component, a circulating pump, a balance tank, a circulating loop, a flow regulating unit, a temperature control unit and a cleaning agent adding unit;
the flow regulating unit comprises a concentrated solution regulating valve and a clear solution regulating valve;
the temperature control unit comprises a tubular heat exchanger, an ice water supply valve, an ice water return valve, a steam valve and a condensate water valve,
the cleaning agent adding unit comprises a pure water valve, an upstream water supply pipe, a concentrated acid valve, an upstream acid supply pipeline, a concentrated alkali valve and an upstream alkali supply pipeline;
the upper top of the membrane component is connected with the top end of the tubular heat exchanger through a pipeline, the upper side of the membrane component is connected with an inlet of the upper top of the clear liquid tank through a shell side clear liquid channel and a clear liquid regulating valve, and the lower end of the clear liquid tank is output through a discharge pipeline and a discharge pump;
the lower end of the raw liquid tank is connected with an inlet at the lower end of the tubular heat exchanger through a feed pipeline sequentially by a feed valve and a feed pump, an outlet at the upper end of the tubular heat exchanger is connected with an inlet at the top end of the membrane component through a pipeline, the side surface at the upper end of the tubular heat exchanger is respectively connected with a steam source through a steam valve by a pipeline and is connected with an ice water supply source through an ice water return valve, and the lower side of the tubular heat exchanger is respectively connected with the ice water supply source through the ice water supply valve by a pipeline and is connected with the steam source through a condensate water valve;
the lower side of the membrane component is connected with a pipeline between the circulating pump and the lower end of the membrane component through a backflushing pipeline and a cleaning backflushing valve; the bottom end of the membrane component is respectively connected with one end of a first valve, one end of a second valve and one end of a discharge valve through pipelines by the circulating pump and the concentrated solution adjusting valve, the other end of the second valve is connected with an inlet at the upper end of the balancing tank through a pipeline, the other end of the first valve is connected with an inlet at the top end of the raw liquid tank, and the other end of the discharge valve is connected with a waste material tank;
the lower end of the balancing tank is connected with a pipeline between the feeding valve and the feeding pump through a tank bottom valve through a pipeline, the top end of the balancing tank is provided with two inlets, one inlet is connected with an inlet at the top end of the stock solution tank through a second valve and a first valve in sequence through a pipeline, the other inlet is connected with a concentrated acid source through a concentrated acid valve and a concentrated alkali source through a concentrated alkali valve respectively through a pipeline, and the other inlet is connected with a pure water source through a pure water valve.
The membrane module comprises a stainless steel membrane shell and a ceramic membrane core. Stainless steel membrane shell material SS316L, sanitary tube processing manufacturing. The filter element is a ceramic membrane with the diameter of 20-50 nanometers. The number and arrangement of membranes are designed according to the processing capacity.
The circulating pump and the loop comprise a circulating pump and a pipeline system. The circulating pump provides flow and pressure required by the membrane module to ensure that the cleaning fluid has proper flow velocity on the surface of the membrane, improve the filtration efficiency and reduce the pollution of protein and fat on the surface of the ceramic membrane. The circulating pump is provided with a frequency converter, and the membrane module is kept to have constant flow rate and working pressure by adjusting the rotating speed of the circulating pump. And monitored by a corresponding pressure gauge.
The balance cylinder system comprises a cylinder body used as a cleaning buffer, a feed centrifugal pump at the outlet of the balance cylinder and a feed valve at the inlet of the balance cylinder. The balance cylinder is provided with a manhole, a ball washer and a liquid level sensor. The centrifugal pump is provided with a frequency converter, so that the rotating speed of the pump can be adjusted, and stable pressure is provided for the membrane component. And a feeding valve at the inlet of the balance tank is used for feeding the raw liquid tank, and when used acid and alkali liquid is supplied to the balance tank, the bottom valve of the balance tank is closed and the used acid and alkali liquid is directly pumped to the ceramic membrane circulation loop by the feeding pump.
The flow regulating unit comprises: a flow sensor and an adjusting valve for the concentrated solution, a flow sensor and an adjusting valve for the clarified solution, and the like. And adjusting the flow of the concentrated solution and the flow of the clear solution of the cleaning solution according to the set recovery yield of the cleaning solution.
The temperature control unit comprises: and a heating unit for heating during cleaning. The heating unit comprises a heat exchanger, a steam supply pipeline, a valve, a pipeline for outputting condensed water and a valve, and the heating unit is needed when the system is cleaned, so that the temperature of the cleaning liquid is increased, and the requirement of a cleaning formula is met.
The cleaning unit comprises a feeding valve and a hose for adding the cleaning agent, a pneumatic diaphragm pump, a flowmeter and a pure water valve. The cleaning agent is added by food-grade concentrated acid and concentrated alkali which share a pneumatic diaphragm pump; and a pure water valve is configured for water top of residual acid and alkali in the pipeline after the addition of the concentrated acid and alkali is finished and water supplement of the balance tank.
The ceramic membrane system can be designed into a semi-automatic or full-automatic control mode, the automation degree is improved, and the risk of manual misoperation can be reduced. The equipment has the advantages of expandable performance, large production capacity range, capability of meeting different production requirements, good linking performance between the single microfiltration machine equipment and other equipment, capability of being closely combined with the front and back processes, optimized process and improved efficiency.
Drawings
Fig. 1 is a schematic structural view of the cleaning solution regeneration ceramic membrane system for dairy plant of the present invention.
Detailed Description
In order to make the technical means, creation features, achievement purposes and functions of the present invention easy to understand, the present invention will be further explained with reference to the specific drawings.
Referring to fig. 1, it can be seen that the cleaning solution regeneration ceramic membrane system for dairy plant of the present invention comprises a ceramic membrane filtration device, a raw liquid tank 15 and a clear liquid tank 16,
the ceramic membrane filtering equipment comprises a membrane module 1, a circulating pump 2, a balance tank 4, a circulating loop, a flow regulating unit, a temperature control unit and a cleaning agent adding unit;
the flow regulating unit comprises a concentrated solution regulating valve 5 and a clear solution regulating valve 6;
the temperature control unit comprises a tubular heat exchanger 10, an ice water supply valve 9a, an ice water return valve 9b, a steam valve 8a and a condensate water valve 8b,
the cleaning agent adding unit comprises a pure water valve 13, an upstream water supply pipe, a concentrated acid valve 14a, an upstream acid supply pipeline, a concentrated alkali valve 14b and an upstream alkali supply pipeline;
the upper top of the membrane module 1 is connected with the top end of the tubular heat exchanger 10 through a pipeline, the upper side of the membrane module 1 is connected with the inlet of the upper top of the clear liquid tank 16 through a shell side clear liquid channel and the clear liquid regulating valve 6, and the lower end of the clear liquid tank 16 is output through a discharge pipeline and the discharge pump 17;
the lower end of the raw liquid tank 15 is connected with an inlet at the lower end of the tubular heat exchanger 10 through a feeding pipeline sequentially by the feeding valve 12 and the feeding pump 3, an outlet at the upper end of the tubular heat exchanger 10 is connected with an inlet at the top end of the membrane module 1 through a pipeline, the side surface of the upper end of the tubular heat exchanger 10 is connected with a steam source through a steam valve 8a and an ice water return valve 9b respectively through pipelines, the lower side of the tubular heat exchanger 10 is connected with an ice water supply source through an ice water supply valve 9a respectively through a pipeline and is connected with the steam source through a condensation water valve 8 b;
the lower side of the membrane module 1 is connected with a pipeline between the circulating pump 2 and the lower end of the membrane module 1 through a backflushing pipeline and the cleaning backflushing valve 11; the bottom end of the membrane module 1 is respectively connected with one end of a first valve 7a, one end of a second valve 7c and one end of a discharge valve 7b through pipelines by the circulating pump 2 and a concentrated solution adjusting valve 5, the other end of the second valve 7c is connected with an inlet at the upper end of the balancing tank 4 through a pipeline, the other end of the first valve 7a is connected with an inlet at the top end of the raw liquid tank 15, and the other end of the discharge valve 7b is connected with a waste material tank;
the lower end of the balance tank 4 is connected with the feeding material (12 and the feeding pump 3) through a pipeline by the tank bottom valve 4a, the top end of the balance tank 4 is provided with two inlets, one inlet is connected with the inlet at the top end of the raw liquid tank 15 through a second valve 7c and a first valve 7a in sequence by pipelines, the other inlet is connected with a concentrated acid source through a concentrated acid valve 14a, connected with a concentrated alkali source through a concentrated alkali valve 14b and connected with a pure water source through a pure water valve 13.
The ceramic membrane system for cleaning liquid regeneration comprises a membrane component 1, a circulating pump 2, a circulating pipeline connected with the membrane component 1 and the circulating pump 2 in series, a balance tank 4, a flow regulating system (comprising a concentrated solution regulating valve 5 and a clear solution regulating valve 6), temperature control units 8-10, a cleaning unit (comprising a pure water valve 13 and a concentrated acid and alkali valve 14), a raw liquid tank 15, a clear liquid tank 16 and the like.
The operation of ceramic membrane systems is largely divided into two main states of production and cleaning. The cleaned equipment can be used for feeding production. The first used turbid cleaning solution is stored in the stock solution tank 15 and the apparatus is in a water circulation state before the turbid cleaning solution enters the apparatus. And (3) opening the feed valve 12, closing the tank bottom valve of the balance tank 4 at the same time, and conveying the turbid cleaning solution into a membrane module circulating system through the variable-frequency constant-pressure conveying of the feed pump 3. The large-flow centrifugal pump 2 in the circulating system enables the turbid cleaning liquid to run in the circulating system in a large flow rate, the flow velocity of 5-7m/s is formed on the membrane surface of the ceramic membrane system 1, the clarified cleaning liquid enters a shell side clarified liquid channel through the filtering surface of the ceramic membrane of 20-50 nanometers under the working conditions of pressure and large flow rate, the flow is controlled by the clarified cleaning liquid regulating valve 6 to be conveyed out of the ceramic membrane system, enters the clear liquid storage tank 16 for standby application, and is pumped to downstream by the discharge pump 17 for use. The tubular heat exchanger 10 in the circulation loop is opened in a cooling mode during production, namely valves 9a and 9b for supplying and returning ice water are opened and closed intermittently, so that the turbid cleaning solution in the equipment is maintained below a set temperature. Discharging clear cleaning liquid, gradually increasing the impurity content of the turbid cleaning liquid, conveying the turbid cleaning liquid out of the system at a set concentration ratio through a regulating valve 5, returning the turbid cleaning liquid to the raw liquid tank 15 for continuous circulation until the produced clear liquid reaches the required recovery yield, generally reaching more than 85%, and finally, discharging the turbid liquid with high impurity content in the raw liquid tank 15. And closing a valve 7a of the turbid liquid return tank 15, simultaneously opening a discharge valve 7b, draining the turbid liquid in the original liquid tank, closing a valve 12 after the tank is empty, opening a tank bottom valve of the balance tank 4, and replenishing water in the balance tank to push off all the turbid liquid in the membrane system. The membrane module system 1 adopts a gradient membrane, the water permeability of the gradient membrane from an inlet to an outlet is increased in a gradient manner, and the difference of the production water flux is caused by the difference of the thicknesses of the supporting layer materials of the membrane at different positions. The structure is used for compensating and balancing the pressure difference between the inside and the outside of the membrane, thereby realizing that the product flux of actual operation is basically kept constant from the membrane inlet to the membrane outlet.
And when the production is finished, closing the feeding valve 12 of the turbid cleaning solution, opening the pure water valve 13 and the tank bottom valve of the balance tank 4, ejecting the materials in the equipment by using water, and after the ejection is finished, switching the equipment through the valves to realize an internal circulation state to prepare for cleaning.
The system is edited with a water flushing program, an acid washing program and an alkali washing program. When the equipment is finished, the water is needed to be flushed before cleaning, the equipment is not used for a long time, and the water is needed to be flushed after the equipment is started. And (3) treating the turbid acid cleaning solution, performing an alkali cleaning procedure, treating the alkali cleaning solution, performing an acid cleaning procedure, and flushing the cleaning solution in the equipment completely by water always after the acid-alkali cleaning is finished. When the water is flushed, the switching valve enables the concentrated solution and the clear solution to be in the ground discharging position, the pure water valve 13 controls the water level of the balance tank 4, the feeding pump 2 and the circulating pump 3 run normally, the concentrated solution adjusting valves 5 and 6 are adjusted to proper opening degrees according to flow rates, and the pre-flushing is carried out for about 5 minutes. And switching a valve to the equipment for circulation, and entering an acid washing step or an alkali washing step. The tubular heat exchanger 10 starts a heating function, namely the corresponding steam valve 8a and the corresponding condensate water valve 8b are opened, the temperature of circulating water in the equipment is gradually increased, the cleaning agent concentrated alkali valve 14 is opened, concentrated acid or concentrated alkali is metered and added into the balancing tank 4 and circulated until the concentration of the dilute acid solution or the dilute alkali solution is uniform, and the pH test paper detects the alkali concentration. When the temperature of the system reaches 70 ℃ required by acid cleaning and 80 ℃ required by alkali cleaning, closing the steam valve 8a and entering cleaning cycle timing. The cleaning backflush valve 11 of the membrane module is periodically switched on and off in short pulses during the whole cleaning process. And (5) finishing the acid washing or alkali washing process after timing, slowly cooling the system to below 40 ℃, and then entering a water flushing program. The waste liquid after water washing and acid-base washing is discharged out of the system through a valve 7 b. The ceramic membrane system is automatically controlled by a computer and a program, has high automation degree, safety and reliability, effectively reduces the labor intensity, and simultaneously avoids the shutdown risk caused by misoperation
The basic principles and the main features of the invention and the advantages of the invention have been shown and described above. It should be understood by those skilled in the art that the present invention is not limited to the above embodiments, and the above embodiments and descriptions are only illustrative of the principles of the present invention, and that various changes and modifications may be made without departing from the spirit and scope of the present invention, and these changes and modifications fall within the scope of the claimed invention.
Claims (1)
1. A ceramic membrane system for regenerating cleaning solution in a dairy plant comprises ceramic membrane filtering equipment, a stock solution tank (15) and a clear solution tank (16),
the ceramic membrane filtering equipment comprises a membrane module (1), a circulating pump (2), a balance tank (4), a circulating loop, a flow regulating unit, a temperature control unit and a cleaning agent adding unit;
the flow regulating unit comprises a concentrated solution regulating valve (5) and a clarified solution regulating valve (6);
the temperature control unit comprises a tubular heat exchanger (10), an ice water supply valve (9a), an ice water return valve (9b), a steam valve (8a) and a condensate water valve (8b),
the cleaning agent adding unit comprises a pure water valve (13), an upstream water supply pipe, a concentrated acid valve (14a), an upstream acid supply pipeline, a concentrated alkali valve (14b) and an upstream alkali supply pipeline;
the upper top of the membrane component (1) is connected with the top end of the tubular heat exchanger (10) through a pipeline, the upper side of the membrane component (1) is connected with an inlet of the upper top of the clear liquid tank (16) through a shell side clear liquid channel and the clear liquid regulating valve (6), and the lower end of the clear liquid tank (16) is output through a discharge pipeline and a discharge pump (17);
the lower end of the raw liquid tank (15) is connected with an inlet at the lower end of the tubular heat exchanger (10) through a feed pipeline sequentially by a feed valve (12) and a feed pump (3), an outlet at the upper end of the tubular heat exchanger (10) is connected with an inlet at the top end of the membrane module (1) through a pipeline, the side surface of the upper end of the tubular heat exchanger (10) is connected with a steam source through a steam valve (8a) and an ice water supply source through an ice water return valve (9b) respectively through pipelines, and the lower side of the tubular heat exchanger (10) is connected with the ice water supply source through the ice water supply valve (9a) and the steam source through a condensation water valve (8b) respectively through pipelines;
the lower side of the membrane component (1) is connected with a pipeline between the circulating pump (2) and the lower end of the membrane component (1) through a backflushing pipeline and a cleaning backflushing valve (11); the bottom end of the membrane component (1) is respectively connected with one end of a first valve (7a), one end of a second valve (7c) and one end of a discharge valve (7b) through pipelines by virtue of the circulating pump (2) and the concentrated solution adjusting valve (5), the other end of the second valve (7c) is connected with an inlet at the upper end of the balancing tank (4) through a pipeline, the other end of the first valve (7a) is connected with an inlet at the top end of the raw liquid tank (15), and the other end of the discharge valve (7b) is connected with a waste material tank;
the lower extreme of compensating tank (4) pass through the pipeline tank bottoms valve (4a) with the pipeline between feed valve (12) and feed pump (3) link to each other, the top of compensating tank (4) have two imports, a mouth pass through the pipeline in proper order through second valve (7c), first valve (7a) with the entry at raw material jar (15) top link to each other, another import pass through the pipeline respectively through concentrated acid valve (14a) link to each other with concentrated acid source, through concentrated alkali valve (14b) link to each other with concentrated alkali source, through pure water valve (13) link to each other with pure water source.
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| CN202021000792.XU CN212640033U (en) | 2020-06-04 | 2020-06-04 | Membrane system for cleaning fluid regeneration of dairy |
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| CN202021000792.XU CN212640033U (en) | 2020-06-04 | 2020-06-04 | Membrane system for cleaning fluid regeneration of dairy |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113274884A (en) * | 2021-05-25 | 2021-08-20 | 重庆中轻装备有限公司 | Activated carbon ceramic membrane cross-flow filtration system and filtration backwashing process |
| CN113441011A (en) * | 2021-07-20 | 2021-09-28 | 合肥科锐特环保工程有限公司 | Gelatin film treatment facility |
| CN114432891A (en) * | 2022-03-03 | 2022-05-06 | 广西大学 | Processing method for camellia oil filtered by ceramic membrane |
| CN115090117A (en) * | 2022-08-25 | 2022-09-23 | 常州合全药业有限公司 | Solvent-resistant ceramic membrane filtering device and process |
-
2020
- 2020-06-04 CN CN202021000792.XU patent/CN212640033U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113274884A (en) * | 2021-05-25 | 2021-08-20 | 重庆中轻装备有限公司 | Activated carbon ceramic membrane cross-flow filtration system and filtration backwashing process |
| CN113441011A (en) * | 2021-07-20 | 2021-09-28 | 合肥科锐特环保工程有限公司 | Gelatin film treatment facility |
| CN114432891A (en) * | 2022-03-03 | 2022-05-06 | 广西大学 | Processing method for camellia oil filtered by ceramic membrane |
| CN115090117A (en) * | 2022-08-25 | 2022-09-23 | 常州合全药业有限公司 | Solvent-resistant ceramic membrane filtering device and process |
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