CN109603280A - A kind of cold and hot double filtration systems - Google Patents
A kind of cold and hot double filtration systems Download PDFInfo
- Publication number
- CN109603280A CN109603280A CN201910131624.XA CN201910131624A CN109603280A CN 109603280 A CN109603280 A CN 109603280A CN 201910131624 A CN201910131624 A CN 201910131624A CN 109603280 A CN109603280 A CN 109603280A
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- filter
- pipeline
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- 238000001914 filtration Methods 0.000 title claims abstract description 154
- 238000005520 cutting process Methods 0.000 claims abstract description 40
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims abstract description 21
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 17
- 238000005057 refrigeration Methods 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 26
- 239000003507 refrigerant Substances 0.000 claims description 15
- 238000001035 drying Methods 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 10
- 239000002826 coolant Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000007710 freezing Methods 0.000 abstract description 2
- 230000008014 freezing Effects 0.000 abstract description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 2
- 239000011707 mineral Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 5
- 125000004122 cyclic group Chemical group 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940004975 interceptor Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/16—Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/02—Combinations of filters of different kinds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D37/00—Processes of filtration
- B01D37/04—Controlling the filtration
- B01D37/046—Controlling the filtration by pressure measuring
Abstract
The present invention is to provide a kind of cold and hot double filtration systems, including refrigeration system Q1, feed liquor system, cooling recirculation system, coolant circulating system, cooling system, filtration system, A recycle stream cutting system, B recycle stream cutting system, filtering type interceptor C3 mend warm system and the warm system of circulation benefit, A feed liquor system, the heating agent circulatory system, heat energy circulating system, ramp cycle system, A filtration system, AA recycle stream cutting system, BB recycle stream cutting system, filtering type interceptor C3C mend warm system and the warm system of A circulation benefit；Present system craft science is practical, has hot and cold filtering function, realizes Rapid Cleaning and continuous filtering, has banned the freezing and filtering system with drainage medium, saves mineral resources, clean and environmental protection.
Description
Technical field
The present invention relates to the cold and hot double filtration systems of one of filtering industry.
Background technique
Currently, in the filtering of the industries liquid such as medicine, chemical industry, light industry, drink, there is many filter type and clear in the market
Technique is washed, after filtering and the discharge of a large amount of mixture is remained every time etc. and pollutes, resource is non-renewable；Filter in the market
Group has much room for improvement in cleaning and continuous filtering.
Summary of the invention
To solve the above-mentioned problems, the object of the present invention is to provide easy to operate, the easy-to-use cold and hot double filtration systems of one kind,
The system process science is practical, has hot and cold filtering function, realizes Rapid Cleaning and continuous filtering.
The cold and hot double filtration systems of one kind, comprising: refrigeration system Q1, feed liquor system, cooling recirculation system, refrigerant circulation
System, down cycles system, filtration system, A recycle stream cutting system, B recycle stream cutting system, filtering type interceptor C3 mend warm system
Warm system, A feed liquor system, the heating agent circulatory system, heat energy circulating system, ramp cycle system, A filtration system, AA are mended with circulation
Recycle stream cutting system, BB recycle stream cutting system, filtering type interceptor C3C mend warm system and A circulation mends warm system；
Wherein the refrigeration system Q1 includes explosion-proof compressor, condenser, evaporator, gas-liquid separator, expansion valve, dry filter
Device etc. forms refrigerating circuit by piping connection；The feed liquor system includes valve A1, shield filter C1, liquid feeding pump H1, valve A2, one
Secondary exchanger W1, second compensation exchanger W2, valve A3, filter pump H2, valve A4, filter C2, valve A5, refined filtration pump H3, valve A6, essence
Filter C4, valve B1, circulating pump H4, valve B2, filtering type interceptor C3, connect to form feed liquor circuit by pipeline；The cooling follows
Loop system includes cooling tower systems Q2, valve Q3, cooling pump H5, the condenser, exchanger K6, valve Q4, connects shape by pipeline
At cooling circuit；The coolant circulating system includes refrigerant tank Q7, valve Q6, the evaporator, second compensation exchange
Device W2, refrigerant pump H6, valve Q8, connect to form refrigerant circulation circuit by pipeline；The cooling system circulation system includes the feed liquor
Pump H1, the valve A2, an exchanger W1, the second compensation exchanger W2, the valve A3, the filter pump H2, institute
State valve A4, the filter C2, the valve A5, the refined filtration pump H3, the valve A6, the strainer C4, the primary exchange
Device W1, transmissometer W3, valve A8, connect to form down cycles circuit by pipeline；The filtration system includes the valve A1, described
Protect filter C1, the liquid feeding pump H1, the valve A2, an exchanger W1, the second compensation exchanger W2, the valve
A3, the filter pump H2, the valve A4, the filter C2, the valve A5, the refined filtration pump H3, the valve A6, the refined filtration
Machine C4, an exchanger W1, the transmissometer W3, valve A7, connect to form filtration circuit by pipeline；The A recycle stream
Cutting system includes the filter C2, the valve B1, the circulating pump H4, the valve B2, the filtering type interceptor C3, valve
B3 connects to form A recycle stream switchback road by pipeline；The B recycle stream cutting system includes the strainer C4, valve B9, described
Circulating pump H4, the valve B2, the filtering type interceptor C3, valve B8, connect to form B recycle stream switchback road by pipeline；It is described
It includes valve B6, the circulating pump H4, the valve B2, the filtering type interceptor C3, valve B4 that filtering type interceptor C3, which mends warm system,
With exchanger W6, connect to form filtering type interceptor C3 benefit temperature loops by pipeline；It includes described cold that the circulation, which mends warm system,
Matchmaker's tank Q7, valve E7, pump E8, the exchanger W6 and valve E6 connect to form circulation benefit temperature loops by pipeline；
The A feed liquor system includes valve A1A, shield filter C1C, liquid feeding pump H1H, valve A2A, an exchanger W1W, second compensation friendship
Parallel operation W2W, valve A3A, filter pump H2H, valve A4A, filter C2C, valve A5A, refined filtration pump H3H, valve A6A, strainer C4C, valve
B1B, circulating pump H4H, valve B2B, filtering type interceptor C3C, connect to form A feed liquor circuit by pipeline；The heating agent cyclic system
System includes heating agent tank F8, valve Q8Q, heat medium pump H6H, second compensation exchanger W2W, the exchanger K6, exchanger W7 and valve F3,
It connects to form heating agent circulation loop by pipeline；The heat energy circulating system includes heat source V1, valve F1, pump F7, the exchanger
W7, valve F2, connect to form heat circulation circuit by pipeline；The ramp cycle system includes the liquid feeding pump H1H, the valve
A2A, an exchanger W1W, the second compensation exchanger W2W, the valve A3A, the filter pump H2H, the valve
A4A, the filter C2C, the valve A5A, the refined filtration pump H3H, the valve A6A, the strainer C4C, the primary friendship
Parallel operation W1W, transmissometer W3W, valve A8A, connect to form ramp cycle circuit by pipeline；The A filtration system includes the valve
A1A, the shield filter C1C, the liquid feeding pump H1H, the valve A2A, an exchanger W1W, second compensation exchange
Device W2W, the valve A3A, the filter pump H2H, the valve A4A, the filter C2C, the valve A5A, refined filtration pump
H3H, the valve A6A, the strainer C4C, an exchanger W1W, the transmissometer W3W, valve A7A, are connected by pipeline
It connects to form A filtration circuit；The AA recycle stream cutting system include the filter C2C, the valve B1B, the circulating pump H4H,
The valve B2B, the filtering type interceptor C3C, valve B3B, connect to form AA recycle stream switchback road by pipeline；The BB circulation
Stream cutting system include the strainer C4C, valve B9B, the circulating pump H4H, the valve B2B, the filtering type interceptor C3C,
Valve B8B connects to form BB recycle stream switchback road by pipeline；It includes valve B6B, institute that the filtering type interceptor C3C, which mends warm system,
Circulating pump H4H, the valve B2B, the filtering type interceptor C3C, valve B4B and exchanger W6W are stated, connects to be formed by pipeline
Filter formula interceptor C3C mends temperature loops；It includes the heating agent tank F8, valve E7E, pump E8E, the exchange that the A circulation, which mends warm system,
Device W6W and valve E6E connects to form A circulation benefit temperature loops by pipeline.
The attachment that filter filtering in the filtration system intercepts increases when needing to clean, and passes through liquid and institute
It states circulation intercepting system to switch in interceptor the attachment logistics, has fast implemented cleaning function, can implement in filtering,
It can also implement after filtration system stopping.
Implement such as in filtering: the pressure of the filtering is set with low voltage value and high-voltage value, and the pressure rise reaches institute
When stating high-voltage value, starting circulation intercepting system cuts the attachment on the filter plate by recycle stream and brings into and intercept in institute
It states in the interceptor in circulation intercepting system；When the pressure value reduction continuously filtered reaches the low voltage value, described in closing
Recycle intercepting system；The low voltage value and the high-voltage value are set according to actual needs.
The principle that stream is cut: impact the filtering surface of filter plate in filter by feed liquor flow velocity, and the impact is detached from
The attachment of interception is filtered on the filtering surface, then passes through the mixing that the circulation intercepting system tape loop has the attachment
Liquid is intercepted the attachment filtration cycle in the interceptor, and the attachment for having fast implemented the filtering surface is detached from, simultaneously
The purpose continuously filtered may be implemented, realize the principle that the stream is cut.
Detailed description of the invention
Fig. 1 is schematic diagram of the invention, and icon is respectively as follows: valve A1, shield filter C1, liquid feeding pump H1, valve A2, primary exchange
Device W1, second compensation exchanger W2, refrigeration system Q1, valve A3, filter pump H2, valve A4, filter C2, valve A5, refined filtration pump H3, valve
A6, strainer C4, transmissometer W3, circulating valve A8, valve A7, valve B1, valve B2, valve B3, valve B4, valve B5, valve B6, valve B7, valve B8, valve
B9, circulating pump H4, filtering type interceptor C3, valve E1, valve E5, valve E6, valve E7, pump E8, exchanger W6, cooling tower systems Q2, valve
Q3, valve Q5, cooling pump H5, valve Q4, exchanger K6, refrigerant tank Q7, valve Q6, refrigerant pump H6, valve Q8, heating agent tank F8, valve Q8Q, heat
Matchmaker pumps H6H, valve F3, exchanger W7, valve F1, pump F7, valve F2, heat source V1；Valve A1A, shield filter C1C, liquid feeding pump H1H, valve A2A,
Exchanger W1W, second compensation exchanger W2W, valve A3A, filter pump H2H, valve A4A, filter C2C, valve A5A, refined filtration pump
H3H, valve A6A, strainer C4C, transmissometer W3W, circulating valve A8A, valve A7A, valve B1B, valve B2B, valve B3B, valve B4B, valve B5B,
Valve B6B, valve B7B, valve B8B, valve B9B, circulating pump H4H, filtering type interceptor C3C, valve E1E, valve E5E, valve E6E, valve E7E, pump
E8E, exchanger W6W.
Specific embodiment
Now in conjunction with attached drawing and foregoing invention content, the present invention is described in further detail.It is an object of the invention to provide one
The cold and hot double filtration systems of kind, present invention process meets science, easy to operate, clean and environmental protection.
Embodiment referring to Fig.1, the cold and hot double filtration systems of one kind, comprising: refrigeration system Q1, feed liquor system, cooling
The circulatory system, coolant circulating system, down cycles system, filtration system, A recycle stream cutting system, B recycle stream cutting system, filtering
Formula interceptor C3 mends warm system and circulation mends warm system, A feed liquor system, the heating agent circulatory system, heat energy circulating system, ramp cycle
System, A filtration system, AA recycle stream cutting system, BB recycle stream cutting system, filtering type interceptor C3C mend warm system and A circulation is mended
Warm system；
Wherein the refrigeration system Q1 includes explosion-proof compressor, condenser, evaporator, gas-liquid separator, expansion valve, dry filter
Device etc. forms refrigerating circuit by piping connection；The feed liquor system includes valve A1, shield filter C1, liquid feeding pump H1, valve A2, one
Secondary exchanger W1, second compensation exchanger W2, valve A3, filter pump H2, valve A4, filter C2, valve A5, refined filtration pump H3, valve A6, essence
Filter C4, valve B1, circulating pump H4, valve B2, filtering type interceptor C3, connect to form feed liquor circuit by pipeline；The cooling follows
Loop system includes cooling tower systems Q2, valve Q3, cooling pump H5, the condenser, exchanger K6, valve Q4, connects shape by pipeline
At cooling circuit；The coolant circulating system includes refrigerant tank Q7, valve Q6, the evaporator, second compensation exchange
Device W2, refrigerant pump H6, valve Q8, connect to form refrigerant circulation circuit by pipeline；The down cycles system includes the feed liquor
Pump H1, the valve A2, an exchanger W1, the second compensation exchanger W2, the valve A3, the filter pump H2, institute
State valve A4, the filter C2, the valve A5, the refined filtration pump H3, the valve A6, the strainer C4, the primary exchange
Device W1, transmissometer W3, valve A8, connect to form down cycles circuit by pipeline；The filtration system includes the valve A1, described
Protect filter C1, the liquid feeding pump H1, the valve A2, an exchanger W1, the second compensation exchanger W2, the valve
A3, the filter pump H2, the valve A4, the filter C2, the valve A5, the refined filtration pump H3, the valve A6, the refined filtration
Machine C4, an exchanger W1, the transmissometer W3, valve A7, connect to form filtration circuit by pipeline；The A recycle stream
Cutting system includes the filter C2, the valve B1, the circulating pump H4, the valve B2, the filtering type interceptor C3, valve
B3 connects to form A recycle stream switchback road by pipeline；The B recycle stream cutting system includes the strainer C4, valve B9, described
Circulating pump H4, the valve B2, the filtering type interceptor C3, valve B8, connect to form B recycle stream switchback road by pipeline；It is described
It includes valve B6, the circulating pump H4, the valve B2, the filtering type interceptor C3, valve B4 that filtering type interceptor C3, which mends warm system,
With exchanger W6, connect to form filtering type interceptor C3 benefit temperature loops by pipeline；It includes described cold that the circulation, which mends warm system,
Matchmaker's tank Q7, valve E7, pump E8, the exchanger W6 and valve E6 connect to form circulation benefit temperature loops by pipeline；
The A feed liquor system includes valve A1A, shield filter C1C, liquid feeding pump H1H, valve A2A, an exchanger W1W, second compensation friendship
Parallel operation W2W, valve A3A, filter pump H2H, valve A4A, filter C2C, valve A5A, refined filtration pump H3H, valve A6A, strainer C4C, valve
B1B, circulating pump H4H, valve B2B, filtering type interceptor C3C, connect to form A feed liquor circuit by pipeline；The heating agent cyclic system
System includes heating agent tank F8, valve Q8Q, heat medium pump H6H, second compensation exchanger W2W, the exchanger K6, exchanger W7 and valve F3,
It connects to form heating agent circulation loop by pipeline；The heat energy circulating system includes heat source V1, valve F1, pump F7, the exchanger
W7, valve F2, connect to form heat circulation circuit by pipeline；The ramp cycle system includes the liquid feeding pump H1H, the valve
A2A, an exchanger W1W, the second compensation exchanger W2W, the valve A3A, the filter pump H2H, the valve
A4A, the filter C2C, the valve A5A, the refined filtration pump H3H, the valve A6A, the strainer C4C, the primary friendship
Parallel operation W1W, transmissometer W3W, valve A8A, connect to form ramp cycle circuit by pipeline；The A filtration system includes the valve
A1A, the shield filter C1C, the liquid feeding pump H1H, the valve A2A, an exchanger W1W, second compensation exchange
Device W2W, the valve A3A, the filter pump H2H, the valve A4A, the filter C2C, the valve A5A, refined filtration pump
H3H, the valve A6A, the strainer C4C, an exchanger W1W, the transmissometer W3W, valve A7A, are connected by pipeline
It connects to form A filtration circuit；The AA recycle stream cutting system include the filter C2C, the valve B1B, the circulating pump H4H,
The valve B2B, the filtering type interceptor C3C, valve B3B, connect to form AA recycle stream switchback road by pipeline；The BB circulation
Stream cutting system include the strainer C4C, valve B9B, the circulating pump H4H, the valve B2B, the filtering type interceptor C3C,
Valve B8B connects to form B recycle stream switchback road by pipeline；It includes valve B6B, institute that the A filtering type interceptor C3C, which mends warm system,
Circulating pump H4H, the valve B2B, the filtering type interceptor C3C, valve B4B and exchanger W6W are stated, connects to be formed by pipeline
Filter formula interceptor C3C mends temperature loops；It includes the heating agent tank F8, valve E7E, pump E8E, the exchange that the A circulation, which mends warm system,
Device W6W and valve E6E connects to form A circulation benefit temperature loops by pipeline.
Concrete operations: after preparatory process is ready, refrigeration filtering starts the cooling recirculation system, the refrigerant circulation system
System and the refrigeration system Q1 start the feed liquor system and are fully loaded with filter raw liquid and close, start the down cycles system later
System cooling closes its system when reaching filtering requirement, starts the filtration system later；The filtration system mode opens in carrying out
It moves the warm system of the circulation benefit and the filtering type interceptor C3 mends warm system and mend warm, the filtering type interceptor C3 stoste
Temperature closes the circulation and mends warm system and filtering type interceptor C3 benefit warm system when reaching filtration temperature；When the filtering
When machine C2 pressure reaches cleaning, starts the A recycle stream cutting system and carry out stream and cut what filter plate filtering surface in the filter C2 intercepted
Attachment is intercepted attachment filtering in the filtering type interceptor C3, the mistake by the A recycle stream cutting system
Filter C2 pressure closes the A recycle stream cutting system after meeting filtering requirement；When the strainer C4 pressure reaches cleaning, open
It moves the B recycle stream cutting system and carries out the attachment that stream cuts filter plate filtering surface interception in the strainer C4, pass through the B recycle stream
Cutting system is intercepted attachment filtering in the filtering type interceptor C3, and the strainer C4 pressure meets filtering requirement
After close the B recycle stream cutting system；On-line cleaning is realized, has ensured continuous filtering.Heating and filtering starts the heating agent and follows
Loop system, the heat energy circulating system start the A feed liquor system and are fully loaded with filter raw liquid and close, start the heating later
Circulatory system heating closes its system when reaching filtering requirement, starts the A filtration system later.The A filtration system mode
In progress, starts the warm system of the A circulation benefit and the filtering type interceptor C3C mends warm system and mend warm, the filtering type
Interceptor C3C stoste temperature closes the A circulation and mends warm system and the filtering type interceptor C3C benefit temperature when reaching filtration temperature
System；When the filter C2C pressure reaches cleaning, starts the AA recycle stream cutting system and carry out stream and cut the filter
Attachment filtering is intercepted the mistake by the AA recycle stream cutting system by the attachment that filter plate filtering surface intercepts in C2C
In filter formula interceptor C3C, the filter C2C pressure closes the AA recycle stream cutting system after meeting filtering requirement；When described
When strainer C4C pressure reaches cleaning, starts the BB recycle stream cutting system and carry out stream and cut filter plate filtering surface in the strainer C4C
Attachment filtering is intercepted the filtering type interceptor C3C by the BB recycle stream cutting system by the attachment of interception
In, the strainer C4C pressure closes the BB recycle stream cutting system after meeting filtering requirement；On-line cleaning is realized, is ensured
Continuous filtering.
The refrigeration filtering single can run, can also run simultaneously according to production requirement with the heating and filtering.
Beneficial effect of the present invention improves work efficiency, reduces production cost, and present invention process meets science, operation letter
It is single, the freezing and filtering system with drainage medium has been banned, mineral resources, clean and environmental protection are saved.
Claims (2)
1. a kind of cold and hot double filtration systems, which is characterized in that including, refrigeration system Q1, feed liquor system, cooling recirculation system, cold
Matchmaker's circulatory system, cooling system, filtration system, A recycle stream cutting system, B recycle stream cutting system, filtering type interceptor C3 mend temperature system
System and circulation mend warm system, A feed liquor system, the heating agent circulatory system, heat energy circulating system, ramp cycle system, A filtration system,
AA recycle stream cutting system, BB recycle stream cutting system, filtering type interceptor C3C mend warm system and A circulation mends warm system.
2. the cold and hot double filtration systems of one kind according to claim 1, which is characterized in that wherein the refrigeration system Q1 includes
Explosion-proof compressor, condenser, evaporator, gas-liquid separator, expansion valve, device for drying and filtering etc. are formed by piping connection and are freezed
Circuit；The feed liquor system includes valve A1, shield filter C1, liquid feeding pump H1, valve A2, an exchanger W1, second compensation exchanger
W2, valve A3, filter pump H2, valve A4, filter C2, valve A5, refined filtration pump H3, valve A6, strainer C4, valve B1, circulating pump H4, valve
B2, filtering type interceptor C3, connect to form feed liquor circuit by pipeline；The cooling recirculation system include cooling tower systems Q2,
Valve Q3, cooling pump H5, the condenser, exchanger K6, valve Q4, connect to form cooling circuit by pipeline；The refrigerant
The circulatory system includes refrigerant tank Q7, valve Q6, the evaporator, the second compensation exchanger W2, refrigerant pump H6, valve Q8, is passed through
Pipeline connects to form refrigerant circulation circuit；The cooling system includes the liquid feeding pump H1, the valve A2, an exchanger
W1, the second compensation exchanger W2, the valve A3, the filter pump H2, the valve A4, the filter C2, the valve A5,
The refined filtration pumps H3, the valve A6, the strainer C4, an exchanger W1, transmissometer W3, valve A8, is connected by pipeline
It connects to form down cycles circuit；The filtration system includes the valve A1, the shield filter C1, the liquid feeding pump H1, the valve
It is A2, an exchanger W1, the second compensation exchanger W2, the valve A3, the filter pump H2, the valve A4, described
It is filter C2, the valve A5, refined filtration pump H3, the valve A6, the strainer C4, an exchanger W1, described turbid
Instrument W3, valve A7 are spent, connects to form filtration circuit by pipeline；The A recycle stream cutting system includes the filter C2, the valve
B1, the circulating pump H4, the valve B2, the filtering type interceptor C3, valve B3, connect to form A recycle stream switchback by pipeline
Road；The B recycle stream cutting system includes that the strainer C4, valve B9, the circulating pump H4, the valve B2, the filtering type block
Machine C3, valve B8 are cut, connects to form B recycle stream switchback road by pipeline；The filtering type interceptor C3 mend warm system include valve B6,
The circulating pump H4, the valve B2, the filtering type interceptor C3, valve B4 and exchanger W6, connect to form filtering by pipeline
Formula interceptor C3 mends temperature loops；The circulation mend warm system include the refrigerant tank Q7, valve E7, pump E8, the exchanger W6 and
Valve E6 connects to form circulation benefit temperature loops by pipeline；The A feed liquor system include valve A1A, shield filter C1C, liquid feeding pump H1H,
Valve A2A, an exchanger W1W, second compensation exchanger W2W, valve A3A, filter pump H2H, valve A4A, filter C2C, valve A5A,
Refined filtration pumps H3H, valve A6A, strainer C4C, valve B1B, circulating pump H4H, valve B2B, filtering type interceptor C3C, is connected by pipeline
Form A feed liquor circuit；The heating agent circulatory system include heating agent tank F8, valve Q8Q, heat medium pump H6H, second compensation exchanger W2W,
The exchanger K6, exchanger W7 and valve F3, connect to form heating agent circulation loop by pipeline；The heat energy circulating system includes
Heat source V1, valve F1, pump F7, the exchanger W7, valve F2, connect to form heat circulation circuit by pipeline；The ramp cycle
System includes the liquid feeding pump H1H, the valve A2A, an exchanger W1W, the second compensation exchanger W2W, described
Valve A3A, the filter pump H2H, the valve A4A, the filter C2C, the valve A5A, the refined filtration pump H3H, the valve
A6A, the strainer C4C, an exchanger W1W, transmissometer W3W, valve A8A, connect to form ramp cycle by pipeline
Circuit；The A filtration system includes the valve A1A, the shield filter C1C, the liquid feeding pump H1H, the valve A2A, described one
Secondary exchanger W1W, the second compensation exchanger W2W, the valve A3A, the filter pump H2H, the valve A4A, the filtering
It is machine C2C, the valve A5A, refined filtration pump H3H, the valve A6A, the strainer C4C, an exchanger W1W, described
Transmissometer W3W, valve A7A, connect to form A filtration circuit by pipeline；The AA recycle stream cutting system includes the filter
C2C, the valve B1B, the circulating pump H4H, the valve B2B, the filtering type interceptor C3C, valve B3B, are connected by pipeline
Form AA recycle stream switchback road；The BB recycle stream cutting system includes the strainer C4C, valve B9B, the circulating pump H4H, institute
Valve B2B, the filtering type interceptor C3C, valve B8B are stated, connects to form BB recycle stream switchback road by pipeline；The filtering type blocks
Cut machine C3C mend warm system include valve B6B, the circulating pump H4H, the valve B2B, the filtering type interceptor C3C, valve B4B and
Exchanger W6W connects to form filtering type interceptor C3C benefit temperature loops by pipeline；It includes the heat that the A circulation, which mends warm system,
Matchmaker's tank F8, valve E7E, pump E8E, the exchanger W6W and valve E6E connect to form A circulation benefit temperature loops by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910131624.XA CN109603280B (en) | 2019-02-22 | 2019-02-22 | Cold and hot two filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910131624.XA CN109603280B (en) | 2019-02-22 | 2019-02-22 | Cold and hot two filtration system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109603280A true CN109603280A (en) | 2019-04-12 |
| CN109603280B CN109603280B (en) | 2022-02-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910131624.XA Active CN109603280B (en) | 2019-02-22 | 2019-02-22 | Cold and hot two filtration system |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201553723U (en) * | 2009-12-14 | 2010-08-18 | 薛爱民 | Wine filtration aiding medium recovery and recycle freezing and filtering device |
| CN108722010A (en) * | 2018-07-16 | 2018-11-02 | 高云芝 | A kind of integrated form freezing and filtering unit |
| CN108759201A (en) * | 2018-07-16 | 2018-11-06 | 高云芝 | A kind of freezing filtration device of double refrigeration systems |
| CN108854239A (en) * | 2018-07-16 | 2018-11-23 | 高云芝 | It is a kind of to freeze double filter devices |
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2019
- 2019-02-22 CN CN201910131624.XA patent/CN109603280B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201553723U (en) * | 2009-12-14 | 2010-08-18 | 薛爱民 | Wine filtration aiding medium recovery and recycle freezing and filtering device |
| CN108722010A (en) * | 2018-07-16 | 2018-11-02 | 高云芝 | A kind of integrated form freezing and filtering unit |
| CN108759201A (en) * | 2018-07-16 | 2018-11-06 | 高云芝 | A kind of freezing filtration device of double refrigeration systems |
| CN108854239A (en) * | 2018-07-16 | 2018-11-23 | 高云芝 | It is a kind of to freeze double filter devices |
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