CN208783722U - A kind of full-automatic desalination system of pot type high-precision low energy consumption - Google Patents
A kind of full-automatic desalination system of pot type high-precision low energy consumption Download PDFInfo
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- CN208783722U CN208783722U CN201820721048.5U CN201820721048U CN208783722U CN 208783722 U CN208783722 U CN 208783722U CN 201820721048 U CN201820721048 U CN 201820721048U CN 208783722 U CN208783722 U CN 208783722U
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- salt water
- desalter
- desalination
- tank
- concentration
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- 238000010612 desalination reaction Methods 0.000 title claims abstract description 83
- 238000005265 energy consumption Methods 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 81
- 150000003839 salts Chemical class 0.000 claims abstract description 77
- 239000000463 material Substances 0.000 claims abstract description 66
- 239000012267 brine Substances 0.000 claims abstract description 53
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 53
- 238000003860 storage Methods 0.000 claims abstract description 27
- 238000002156 mixing Methods 0.000 claims abstract description 26
- 239000012530 fluid Substances 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 20
- 238000001914 filtration Methods 0.000 claims description 15
- 230000008676 import Effects 0.000 claims description 7
- 238000005259 measurement Methods 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- XZPVPNZTYPUODG-UHFFFAOYSA-M sodium;chloride;dihydrate Chemical compound O.O.[Na+].[Cl-] XZPVPNZTYPUODG-UHFFFAOYSA-M 0.000 claims 1
- 230000003247 decreasing effect Effects 0.000 abstract description 4
- 238000004886 process control Methods 0.000 abstract description 2
- 238000011033 desalting Methods 0.000 description 11
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
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- Storage Of Fruits Or Vegetables (AREA)
Abstract
The utility model discloses a kind of full-automatic desalination systems of pot type high-precision low energy consumption, including at least one independent desalter and at least two brine tanks, brine strength in each brine tank is all different, wherein it is connect by pipeline with the inlet of at least one blending tank for storing the brine tank of higher concentration salt water, the discharge port of the blending tank is connect with desalter respectively, each desalination pot bottom is provided with material outlet and the leakage fluid dram for discharging high concentration salt water, the low concentration salt water being discharged by the material outlet of desalter is returned by pipeline in the brine tank of storage low concentration salt water, the brine tank of the storage low concentration salt water is connect by pipeline with the low concentration of salt water inlet on desalter top, the salt water gradually to be successively decreased by concentration successively carries out desalination to material.The utility model device occupied area is small, can improve the process control to material desalination, and salinity control is more accurate, and after desalination salt water concentration it is high, effectively reduce the treating capacity of salt water.
Description
Technical field
The utility model belongs to food processing technology field, in particular to a kind of full-automatic desalination of pot type high-precision low energy consumption
System.
Background technique
At present in food processing and production, it usually needs carry out desalting processing to material, the existing desalination for material is all
It is that material is put into the desalination box body of strip using Desalination machine, hanging plate is conveyed using the material of Desalination machine, by object
Material is sent to output end by input terminal, during material conveys in cabinet, desalination is carried out by the intracorporal salt water of case, in cabinet
Output end is continually fed into clear, and salt water after desalination is discharged by the input terminal of cabinet.The desalination mode of existing Desalination machine is mainly deposited
In following problems:
1, the poor controllability of material desalination processes is stored in Desalination machine since the liquid for desalination all mixes
In cabinet, only with output end into clear water, output end arranges the mode of high concentration salt water, can not be to material during transportation
Desalination controlled, cause the stability of the final desalination of material poor, material salinity consistency is not high.
2, the brine strength of output end discharge is not high, to reach the requirement of the final salinity of material, need to improve Desalination machine
Inflow causes final saline treatment amount to increase, and processing cost is high, the salt water that existing Desalination machine is discharged to improve output end
Concentration, then need to improve the time of material desalting processing in Desalination machine, and to increase the time of processing, then needs to increase desalination
The length of machine, thus the problem for causing occupation area of equipment big, if not increasing the length of Desalination machine, it is ensured that the desalination time is again
The production capacity of equipment can be largely effected on.
3. the material conveying scraper plate cleaning in Desalination machine is difficult, there is larger impact to the hygienic requirements of material production.
Utility model content
The goal of the invention of the utility model is that in view of the above problems, providing one kind can be improved material desalination
The concentration of salt water after the control and desalination of precision, to reduce saline treatment amount, and the pot type high-precision that occupation area of equipment is small
The full-automatic desalination system of low energy consumption and desalination process.
The technical solution of the utility model is achieved in that a kind of full-automatic desalination system of pot type high-precision low energy consumption,
Brine strength it is characterized by comprising at least one independent desalter and at least two brine tanks, in each brine tank
It is all different, wherein the brine tank for storing higher concentration salt water is connected by the inlet of pipeline and at least one blending tank
It connects, the discharge port of the blending tank is connect with desalter respectively, and each desalination pot bottom is provided with material outlet and for arranging
The leakage fluid dram for putting high concentration salt water, the low concentration salt water being discharged by the material outlet of desalter return to storage low concentration by pipeline
In the brine tank of salt water, the brine tank of the storage low concentration salt water passes through the low concentration of salt water inlet of pipeline and desalter top
Connection, the salt water gradually to be successively decreased by concentration successively carry out desalination to material.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, the blending tank and material lifting
Machine connection, be provided with Weighing module on the material elevator and/or blending tank, for enter blending tank in material and
Salt water carries out accurate measurement.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, goes out in the material of the desalter
Splicing filtering temporary storage machine is provided with below mouthful, the material in the desalter is discharged into progress solid-liquid point in splicing filtering temporary storage machine
From the liquid outlet of the splicing filtering temporary storage machine is connect by pipeline with the brine tank for storing low concentration salt water.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, the circulation of the desalination pot bottom
Liquid import forms circulation path by the circulation fluid of circulation desalination pump and desalter outlet connection.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, the splicing filtering temporary storage machine
Liquid outlet is pumped by wash cycles and is connect at the top of desalter.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, sets at the top of the desalter
It is equipped with clear water import.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, in the desalter and salt water
Air intlet is provided at the top of tank, and the desalter and brine tank are controlled to a vacuum pump.
The full-automatic desalination system of pot type high-precision low energy consumption described in the utility model, the brine tank are two,
In one be low concentration of salt water pot, another be middle concentration brine tank, the middle concentration brine tank by pump is connect with blending tank,
The desalination pot bottom is connect by pipeline with middle concentration brine tank, and the liquid outlet of the splicing filtering temporary storage machine passes through pipeline
It is connect with low concentration of salt water pot, the low concentration of salt water pot is connect by pump with the low concentration of salt water inlet of desalter.
The utility model carries out desalination by way of desalter, and the thickness of material accumulation is higher in desalter, same
In the case where production capacity, occupation area of equipment is smaller, into desalter material and salt water quantify, and the mode of desalination is
The salt water gradually to be successively decreased using concentration successively carries out desalination to material, controllable for the brine strength of material desalination every time, greatly
The process control capabilities of material desalination are improved greatly, and salinity control is more accurate, in addition, improving by way of desalination step by step
The concentration of salt water, effectively reduces the treating capacity of salt water, processing cost is lower, and the cleaning of each tank body and pipeline after desalination
It is more convenient, be conducive to the hygienic requirements for meeting food processing.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the structural schematic diagram removed after splicing filtering temporary storage machine in the utility model.
Marked in the figure: 1 is desalter, 2 be blending tank, and 3 be material elevator, and 4 filter temporary storage machine for splicing, and 5 be circulation
Desalination pump, 6 pump for wash cycles, and 7 be low concentration of salt water pot, and 8 be middle concentration brine tank.
Specific embodiment
With reference to the accompanying drawing, the utility model is described in detail.
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain
The utility model is not used to limit the utility model.
As illustrated in fig. 1 and 2, a kind of full-automatic desalination system of pot type high-precision low energy consumption, including at least one is independent de-
Salt cellar 1 and at least two brine tanks, the brine strength in each brine tank are all different, wherein for storing higher concentration salt
The brine tank of water is connect by pipeline with the inlet of at least one blending tank 2, and the blending tank 2 is connect with material elevator 3,
It is provided with Weighing module on the material elevator 3 and/or blending tank 2, for the material and salt water entered in blending tank 2
Accurate measurement is carried out, the discharge port of the blending tank 2 is connect with desalter 1 respectively, and each 1 bottom of desalter is provided with material and goes out
It is temporary to be provided with splicing filtering below the material outlet of the desalter 1 for mouth and the leakage fluid dram for discharging high concentration salt water
Machine 4 is deposited, the material in the desalter 1 is discharged into splicing to filter in temporary storage machine 4 and is separated by solid-liquid separation, and the splicing filtering is temporary
The liquid outlet of machine 4 is connect by pipeline with the brine tank for storing low concentration salt water, i.e., is discharged by the material outlet of desalter 1
Low concentration salt water is returned by pipeline in the brine tank of storage low concentration salt water, and the brine tank of the storage low concentration salt water passes through
Pipeline is connect with the low concentration of salt water inlet on 1 top of desalter, and the top of the desalter 1 is provided with clear water import, passes through
The salt water that concentration is gradually successively decreased successively carries out desalination to material.
In the present embodiment, the brine tank is two, one of them is low concentration of salt water pot 7, another is middle concentration
Brine tank 8, the middle concentration brine tank 8 are connect by pump with blending tank 2, and 1 bottom of desalter passes through pipeline and middle concentration
Brine tank 8 connects, and the liquid outlet of the splicing filtering temporary storage machine 4 is connect by pipeline with low concentration of salt water pot 7, described low dense
Degree brine tank 7 is connect by pump with the low concentration of salt water inlet of desalter 1.Wherein, high salt concentration water concentration be 7-10%, in it is dense
Degree brine strength is 3-7%, and low concentration of salt water concentration is 2-3%, and specific concentration can require to make adaptability according to actual production
Adjustment.
In order to improve desalting effect of the material in desalter, the circulation fluid import of 1 bottom of desalter passes through circulation
Desalination pump 5 and the circulation fluid outlet connection of desalter 1 form circulation path, are increased between material and liquid by the circulation of liquid
Flowing, so that material is flowed in desalination processes, contact of the material with liquid increased, to improve the desalting effect of material
And efficiency.
Wherein, the liquid outlet of splicing filtering temporary storage machine 4 by wash cycles pump 6 with connected at the top of desalter 1,
After desalter completes a material desalination, splicing is filtered in the liquid pump to desalter in temporary storage machine, it is rinsed, phase
It is more convenient to the cleaning of existing Desalination machine, it is more favorable to meet the hygienic requirements of food processing.
In the present embodiment, air intlet, and the desalination are provided at the top of the desalter 1 and brine tank
Tank 1 and brine tank are controlled to a vacuum pump.The desalter realize under vacuum conditions charging and desalination, brine tank also by
Vacuum feed liquor, can be improved the conveying of material and liquid, and be conducive to the desalination of material.
Using the desalination process of the utility model desalination system, comprising the following steps:
A) by the brine pump in middle concentration brine tank to blending tank, material is sent into blending tank, object after measuring by elevator
Material is adequately mixed in blending tank with the salt water of middle concentration.
B) mixed material, which is fed through in desalter, carries out desalting processing, the high salt concentration generated after desalting processing
Water is discharged by the leakage fluid dram for discharging high concentration salt water that desalination pot bottom is arranged, and the high concentration salt water of discharge is collected
Processing or be used for material Pretreatment Line, wherein the discharge of high concentration salt water be in desalter salinometer and/or desalination
Time control.
C) by the salt water in low concentration of salt water pot by desalter low concentration of salt water inlet be sent into, and with the object in desalter
Material mixing continues desalting processing, and the middle concentration salt water generated after desalting processing passes through in concentration brine tank in pipeline feeding
It is stored, wherein the inflow of low concentration salt water is controlled by the fluid level controller in desalter, and the discharge of middle concentration salt water
Be in desalter salinometer and/or the desalination time control.
D) clear water is sent by the clear water import at the top of desalter, and is mixed with the material in desalter and continues desalination
Processing opens the material outlet of desalination pot bottom, material is drained into splicing filtering temporary storage machine, through splicing after desalting processing
The solid material of filter temporary storage machine filtering enters rear process and continues with, and the low concentration salt water filtered out is sent into low concentration by pipeline
It is stored in brine tank.
Wherein, for the desalter by the way of vacuum desalting and vacuum feed, desalter passes through vacuum before charging
Mixed material in blending tank is sucked into desalter by vacuum and is carried out at desalination by pump by vacuum pumping state in desalter
It manages, the desalting processing in desalter also carries out under vacuum conditions, and the salt water in low concentration of salt water pot enters the mode of desalter
Also by the vacuum state sucking in desalter, the low concentration of salt water pot and middle concentration brine tank also by the way of vacuum into
Liquid.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model
Protection scope within.
Claims (8)
1. a kind of full-automatic desalination system of pot type high-precision low energy consumption, it is characterised in that: including at least one independent desalter
(1) and at least two brine tanks, the brine strength in each brine tank is all different, wherein for storing higher concentration salt water
Brine tank connect with the inlet of at least one blending tank (2) by pipeline, the discharge port of the blending tank (2) respectively with take off
Salt cellar (1) connection, each desalter (1) bottom are provided with material outlet and the leakage fluid dram for discharging high concentration salt water, by
The low concentration salt water of the material outlet discharge of desalter (1) is returned by pipeline in the brine tank of storage low concentration salt water, described
The brine tank of storage low concentration salt water is connect by pipeline with the low concentration of salt water inlet on desalter (1) top, by concentration by
The salt water gradually to successively decrease successively carries out desalination to material.
2. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 1, it is characterised in that: the blending tank
(2) it is connect with material elevator (3), is provided with Weighing module on the material elevator (3) and/or blending tank (2), is used for
Accurate measurement is carried out to the material and salt water that enter in blending tank (2).
3. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 1, it is characterised in that: in the desalination
Splicing filtering temporary storage machine (4) is provided with below the material outlet of tank (1), the material in the desalter (1) is discharged into splicing
It is separated by solid-liquid separation in filter temporary storage machine (4), the liquid outlet of splicing filtering temporary storage machine (4) passes through pipeline and storage low concentration
The brine tank of salt water connects.
4. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 1, it is characterised in that: the desalter
(1) the circulation fluid import of bottom forms circulation path by the circulation fluid outlet connection of circulation desalination pump (5) and desalter (1).
5. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 3, it is characterised in that: the splicing
The liquid outlet of temporary storage machine (4) is filtered by connecting at the top of wash cycles pump (6) and desalter (1).
6. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 1, it is characterised in that: in the desalination
Tank is provided with clear water import at the top of (1).
7. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 1, it is characterised in that: in the desalination
Air intlet is provided at the top of tank (1) and brine tank, and the desalter (1) and brine tank connect with vacuum pump
It connects.
8. the full-automatic desalination system of pot type high-precision low energy consumption according to claim 3 or 5, it is characterised in that: the salt
Water pot is two, one of them is low concentration of salt water pot (7), another is middle concentration brine tank (8), the middle concentration brine tank
(8) it is connect by pump with blending tank (2), desalter (1) bottom is connect by pipeline with middle concentration brine tank (8), described
The liquid outlet of splicing filtering temporary storage machine (4) is connect by pipeline with low concentration of salt water pot (7), the low concentration of salt water pot (7)
It is connect by pumping with the low concentration of salt water inlet of desalter (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820721048.5U CN208783722U (en) | 2018-05-15 | 2018-05-15 | A kind of full-automatic desalination system of pot type high-precision low energy consumption |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820721048.5U CN208783722U (en) | 2018-05-15 | 2018-05-15 | A kind of full-automatic desalination system of pot type high-precision low energy consumption |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208783722U true CN208783722U (en) | 2019-04-26 |
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ID=66200049
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820721048.5U Active CN208783722U (en) | 2018-05-15 | 2018-05-15 | A kind of full-automatic desalination system of pot type high-precision low energy consumption |
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| Country | Link |
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| CN (1) | CN208783722U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108477470A (en) * | 2018-05-15 | 2018-09-04 | 成都海科机械设备制造有限公司 | A kind of full-automatic desalination system of pot type high-precision low energy consumption and desalination process |
-
2018
- 2018-05-15 CN CN201820721048.5U patent/CN208783722U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108477470A (en) * | 2018-05-15 | 2018-09-04 | 成都海科机械设备制造有限公司 | A kind of full-automatic desalination system of pot type high-precision low energy consumption and desalination process |
| CN108477470B (en) * | 2018-05-15 | 2024-04-16 | 成都海科机械设备制造有限公司 | Tank type high-precision low-energy-consumption full-automatic desalination system and desalination method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Tank-type high-precision low-energy-consumption automatic desalting system and desalting method Effective date of registration: 20190827 Granted publication date: 20190426 Pledgee: Agricultural Bank of China Limited by Share Ltd. Chengdu Wenjiang branch Pledgor: CHENGDU HAIKE MECHANICAL EQUIPMENT MANUFACTURING Co.,Ltd. Registration number: Y2019510000015 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Tank-type high-precision low-energy-consumption automatic desalting system and desalting method Effective date of registration: 20190827 Granted publication date: 20190426 Pledgee: Agricultural Bank of China Limited by Share Ltd. Chengdu Wenjiang branch Pledgor: CHENGDU HAIKE MECHANICAL EQUIPMENT MANUFACTURING Co.,Ltd. Registration number: Y2019510000015 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20190426 Pledgee: Agricultural Bank of China Limited by Share Ltd. Chengdu Wenjiang branch Pledgor: CHENGDU HAIKE MECHANICAL EQUIPMENT MANUFACTURING Co.,Ltd. Registration number: Y2019510000015 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |