CN107188925A - A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology - Google Patents
A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology Download PDFInfo
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- CN107188925A CN107188925A CN201710345023.XA CN201710345023A CN107188925A CN 107188925 A CN107188925 A CN 107188925A CN 201710345023 A CN201710345023 A CN 201710345023A CN 107188925 A CN107188925 A CN 107188925A
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- fresh air
- negative pressure
- heat pump
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- 238000000034 method Methods 0.000 title claims abstract description 43
- 238000005516 engineering process Methods 0.000 title claims abstract description 25
- 108010082495 Dietary Plant Proteins Proteins 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 67
- 238000000605 extraction Methods 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 230000001954 sterilising effect Effects 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 8
- 230000003020 moisturizing effect Effects 0.000 claims abstract description 7
- 238000002347 injection Methods 0.000 claims description 30
- 239000007924 injection Substances 0.000 claims description 30
- 230000006835 compression Effects 0.000 claims description 28
- 238000007906 compression Methods 0.000 claims description 28
- 238000000926 separation method Methods 0.000 claims description 12
- 238000005086 pumping Methods 0.000 claims description 9
- 244000046052 Phaseolus vulgaris Species 0.000 claims description 8
- 235000010627 Phaseolus vulgaris Nutrition 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 8
- 235000013336 milk Nutrition 0.000 claims description 8
- 239000008267 milk Substances 0.000 claims description 8
- 210000004080 milk Anatomy 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 7
- 238000007701 flash-distillation Methods 0.000 claims description 7
- 210000004907 gland Anatomy 0.000 claims description 7
- 238000001694 spray drying Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 238000004659 sterilization and disinfection Methods 0.000 claims description 5
- 239000003513 alkali Substances 0.000 claims description 4
- 210000000481 breast Anatomy 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 238000005070 sampling Methods 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 239000002585 base Substances 0.000 claims 1
- 230000014616 translation Effects 0.000 abstract description 5
- 239000002918 waste heat Substances 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 6
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 108010073771 Soybean Proteins Proteins 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000164 protein isolation Methods 0.000 description 1
- 230000003946 protein process Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000019710 soybean protein Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, belong to vegetable protein production technology and industrial energy saving technical field, in the extraction produced for vegetable protein and process for sterilizing, high temperature feed liquid enters the problem of a large amount of secondary low-voltage steam and its waste heat that shwoot goes out after flash tank are wasted, pressurization heating is carried out to flash-off steam using HEAT PUMP BASED ON EJECTING PRINCIPLE technology, and it is sent to the air inlet progress fresh air preheating of drying process fresh air, condensate is sent to solidifying water pot by condensate line, solidifying water pot top is provided with vacuum extractor, solidifying water pot bottom condenses water out and is connected with condensate pump, condensate is sent to technique moisturizing by condensate pump, it is achieved thereby that the water resource and residual heat resources of flash-off steam are by reuse.
Description
Technical field
The present invention relates to a kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, belong to plant egg
White production technology and industrial energy saving technical field.
Background technology
Following flow is generally used using the vegetable protein production of soybean protein isolation technics：Extraction process：The AA+ that adds water expects
<1：9>——》Separation ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》Newborn acid adding is entered
Row acid is heavy ---》It is separated into curdled milk+beans stripping water（Sampling water）——》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization
（130~150 DEG C）——》Flash distillation, cooling（65~75 DEG C）——》Spray drying ---》Albumen powder discharges.
In the extraction of vegetable protein production and process for sterilizing, material liquid turns into high temperature feed liquid after wet sterilization, enters back into
Flash tank is cooled, concentrated, wherein the indirect steam in flash tank because its pressure and temperature it is relatively low, generally in condenser by
Cooling water system is condensed and is dissipated waste heat amount and is wasted into surrounding air, and its condensate is also generally arranged
Enter cesspool.
The content of the invention
The purpose of the present invention and task are, in the extraction produced for vegetable protein and process for sterilizing, and high temperature feed liquid enters
The problem of a large amount of secondary low-voltage steam and its waste heat that shwoot goes out after flash tank are wasted, using HEAT PUMP BASED ON EJECTING PRINCIPLE technology
Pressurization heating is carried out to flash-off steam, and is sent to the air inlet of drying process fresh air carrying out fresh air preheating, and reclaim its condensate
Technique moisturizing is sent to, reaches the water resource and residual heat resources of flash-off steam by the purpose of reuse.
The present invention specific descriptions be：A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology,
The pressure and temperature of flash-off steam is improved using HEAT PUMP BASED ON EJECTING PRINCIPLE technology, and by its contained water resource and residual heat resources fully recovering
In technique, it is characterised in that be somebody's turn to do the vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology and drawn using split type
Formula heat pump is penetrated, the split type HEAT PUMP BASED ON EJECTING PRINCIPLE system includes injection type both vapor compression module, negative pressure steam condenser-fresh air
The connecting line of warm-up block and condensate postpositive disposal reuse module and correlation is constituted with pipe fitting, wherein injection type both vapor compression
Module includes injection type vapour compression unit 4, driving steam and enters steam control valve 2, low pressure admission pipe 3, gland steam exhauster 5, negative pressure steam
Condenser-fresh air preheating module includes negative pressure steam condenser-fresh air preheating device 6, solidifying water pot 7, vacuum pumping pump 8, condensate pump 9
Composition, wherein the side of original flash tank 1 is provided with high temperature feed liquid A import, bottom is provided with concentration feed liquid B outlet, top
Be provided with flash-off steam outlet, the flash-off steam outlet is connected with original condenser, and with newly-increased injection type both vapor compression module
Injection type vapour compression unit 4 low pressure admission pipe 3 be connected, the driving steam inlet of injection type vapour compression unit 4 is set
It is equipped with driving steam and enters steam control valve 2, gland steam exhauster 5 and the negative pressure steam condenser-fresh air preheating of injection type vapour compression unit 4
The air intake of device 6 is connected, and the delivery port of negative pressure steam condenser-fresh air preheating device 6 is connected with the water inlet of solidifying water pot 7, coagulates water
The on-condensible gas exhaust outlet on the top of tank 7 is connected with the air inlet of vacuum pumping pump 8, exhaust outlet and the surrounding air phase of vacuum pumping pump 8
Logical, the delivery port of the solidifying bottom of water pot 7 is connected with the water inlet of condensate pump 9, delivery port and the rearmounted place of condensate of condensate pump 9
The water inlet for managing reuse module 10 is connected, and the delivery port of condensate postpositive disposal reuse module 10 is communicated with technique moisturizing to be connected,
The inlet side of negative pressure steam condenser-fresh air preheating device 6 is communicated with outdoor air, air side and original steam air heater or
Conduction oil air heater is connected.
The process flow, be by existing conventional flowsheet：Extraction process add water AA+ material<1：9>——》Point
From ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》It is heavy that newborn acid adding carries out acid ---》
It is separated into curdled milk+beans stripping water sampling water ---》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization 130~150
℃——》Flash distillation, 65~75 DEG C of cooling ---》Spray drying ---》Albumen powder discharges, wherein the air intake heater being spray-dried
Skill flow is：Outdoor fresh air ---》Steam heater or hotline heater ---》Drying tower；New technological flow is adjusted to, its
The part of middle change is：The indirect steam after flash distillation, 65~75 DEG C of cooling in existing common process；With a part of high drive
Steam ---》Injection type vapour compression unit 4 ---》Negative pressure steam condenser-fresh air preheating device 6 ---》Solidifying water pot 7 ---》
Condensate feeding condensate postpositive disposal reuse module 16 after separation ---》Extraction process adds water the AA and/or BB that adds water；Wherein
The air intake heating technological process of spray drying is adjusted to：Outdoor fresh air ---》Negative pressure steam condenser-fresh air preheating device 6 ---》
Steam heater or hotline heater ---》Drying tower.
Injection type vapour compression unit 4 uses negative pressure steam type injection pump configuration.
Driving steam enters steam control valve 2 and uses motorized adjustment valve arrangement.
Negative pressure steam condenser-fresh air preheating device 6 is vertically arranged using heat-exchanging tube bundle.
Negative pressure steam condenser-fresh air preheating device 6 uses heat-exchanging tube bundle lateral arrangement.
Negative pressure steam condenser-fresh air preheating device 6 is using pressure-bearing type or longitudinal water and on-condensible gas isolating construction.
Part and pipeline composition integral structure included by negative pressure steam condenser-fresh air preheating module, also can split
Formula is set.
The present invention solve in vegetable protein production the water resource of extraction and flash tank indirect steam in process for sterilizing with
The problem of residual heat resources are recycled, carries out pressurization heating, and be sent to back tender using HEAT PUMP BASED ON EJECTING PRINCIPLE technology to flash-off steam
The air inlet of skill fresh air carries out fresh air preheating, and condensate is sent to technique moisturizing, it is achieved thereby that the water resource of flash-off steam and
Residual heat resources are by reuse.
Meanwhile, technical method and its device and engineering construction scheme designed by the present invention, also can further genralrlization arrive it
In the similar technique processing procedure of its industry, with more common industry application value and economic results in society.
Brief description of the drawings
Fig. 1 is the system schematic of the present invention.
Each unit number and title are as follows in Fig. 1.
Flash tank 1, driving steam enter steam control valve 2, low pressure admission pipe 3, injection type vapour compression unit 4, gland steam exhauster 5,
Negative pressure steam condenser-fresh air preheating device 6, solidifying water pot 7, vacuum pumping pump 8, condensate pump 9, condensate postpositive disposal reuse module
10th, high temperature feed liquid A, concentration feed liquid B, the indirect steam towards condenser（C）, technique moisturizing（D）, on-condensible gas exhaust（E）, it is new
Wind preheats air-out（F）, fresh air preheating air intake（G）, driving steam（H）.
Embodiment
Fig. 1 is the system schematic of the present invention.
The specific embodiment of the present invention is as follows：A kind of vegetable protein flash-off steam reuse side based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology
Method, using split type HEAT PUMP BASED ON EJECTING PRINCIPLE system, the split type HEAT PUMP BASED ON EJECTING PRINCIPLE system includes injection type both vapor compression module, negative pressure
The connecting line of steam condenser-fresh air preheating module and condensate postpositive disposal reuse module and correlation is constituted with pipe fitting, its
Middle injection type both vapor compression module include injection type vapour compression unit 4, driving steam enter steam control valve 2, low pressure admission pipe 3,
Gland steam exhauster 5, negative pressure steam condenser-fresh air preheating module includes negative pressure steam condenser-fresh air preheating device 6, solidifying water pot 7, taken out
Vavuum pump 8, condensate pump 9 are constituted, wherein the side of original flash tank 1 is provided with high temperature feed liquid A import, bottom is provided with concentration
Feed liquid B outlet, top is provided with flash-off steam outlet, and flash-off steam outlet is connected with original condenser, and draws with newly-increased
The low pressure admission pipe 3 for penetrating the injection type vapour compression unit 4 of formula both vapor compression module is connected, injection type vapour compression unit 4
Driving steam inlet is provided with driving steam and enters steam control valve 2, and gland steam exhauster 5 and the negative pressure of injection type vapour compression unit 4 are steamed
The air intake of vapour condenser-fresh air preheating device 6 is connected, the delivery port of negative pressure steam condenser-fresh air preheating device 6 and solidifying water pot 7
Water inlet be connected, the on-condensible gas exhaust outlet on the solidifying top of water pot 7 is connected with the air inlet of vacuum pumping pump 8, the row of vacuum pumping pump 8
Gas port is communicated with surrounding air, and the delivery port of the solidifying bottom of water pot 7 is connected with the water inlet of condensate pump 9, the water outlet of condensate pump 9
Mouth is connected with the water inlet of condensate postpositive disposal reuse module 10, the delivery port and work of condensate postpositive disposal reuse module 10
Skill moisturizing communicates connected, and the inlet side of negative pressure steam condenser-fresh air preheating device 6 is communicated with outdoor air, air side with it is original
Steam air heater or conduction oil air heater are connected.
The process flow, be by existing conventional flowsheet：Extraction process add water AA+ material<1：9>——》Point
From ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》It is heavy that newborn acid adding carries out acid ---》
It is separated into curdled milk+beans stripping water sampling water ---》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization 130~150
℃——》Flash distillation, 65~75 DEG C of cooling ---》Spray drying ---》Albumen powder discharges, wherein the air intake heater being spray-dried
Skill flow is：Outdoor fresh air ---》Steam heater or hotline heater ---》Drying tower；New technological flow is adjusted to, its
The part of middle change is：The indirect steam after flash distillation, 65~75 DEG C of cooling in existing common process；With a part of high drive
Steam ---》Injection type vapour compression unit 4 ---》Negative pressure steam condenser-fresh air preheating device 6 ---》Solidifying water pot 7 ---》
Condensate feeding condensate postpositive disposal reuse module 16 after separation ---》Extraction process adds water the AA and/or BB that adds water；Wherein
The air intake heating technological process of spray drying is adjusted to：Outdoor fresh air ---》Negative pressure steam condenser-fresh air preheating device 6 ---》
Steam heater or hotline heater ---》Drying tower.
Injection type vapour compression unit 4 uses negative pressure steam type injection pump configuration.
Driving steam enters steam control valve 2 and uses motorized adjustment valve arrangement.
Negative pressure steam condenser-fresh air preheating device 6 is vertically arranged using heat-exchanging tube bundle.
Negative pressure steam condenser-fresh air preheating device 6 is using pressure-bearing type water and on-condensible gas isolating construction.
Part and pipeline composition integral structure included by negative pressure steam condenser-fresh air preheating module.
It should be noted that how the present invention solves indirect steam in flash tank using HEAT PUMP BASED ON EJECTING PRINCIPLE technology if being proposed
The method of water resource and residual heat resources reuse problem, and according to this conceptual solutions can have different specific implementation measures and
The specific implementation device of different structure, above-mentioned embodiment is only a kind of, any other like letter therein
The embodiment of monotropic shape, uses integral type or split-type structural such as negative pressure steam condenser-fresh air preheating module；Set
Or be not provided with condensate postpositive disposal reuse module 10 or carry out mode of texturing that average expert personage is contemplated that etc., or will
The technical approach is applied to other similar application occasions in addition to vegetable protein production industry with same or analogous structure,
Fall into protection scope of the present invention.
Claims (8)
1. a kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, is improved using HEAT PUMP BASED ON EJECTING PRINCIPLE technology
The pressure and temperature of flash-off steam, and by its contained water resource and residual heat resources fully recovering in technique, it is characterised in that the base
Split type HEAT PUMP BASED ON EJECTING PRINCIPLE system is used in the vegetable protein flash-off steam reuse method of HEAT PUMP BASED ON EJECTING PRINCIPLE technology, this is split type to draw
Penetrating formula heat pump includes injection type both vapor compression module, negative pressure steam condenser-fresh air preheating module and the rearmounted place of condensate
The connecting line for managing reuse module and correlation is constituted with pipe fitting, and wherein injection type both vapor compression module includes injection type both vapor compression
Device（4）, driving steam enter steam control valve（2）, low pressure admission pipe（3）, gland steam exhauster（5）, negative pressure steam condenser-fresh air preheating
Module includes negative pressure steam condenser-fresh air preheating device（6）, solidifying water pot（7）, vacuum pumping pump（8）, condensate pump（9）Composition, its
In original flash tank（1）Side is provided with high temperature feed liquid（A）Import, bottom is provided with concentration feed liquid（B）Outlet, top is set
Be equipped with flash-off steam outlet, the flash-off steam outlet is connected with original condenser, and with newly-increased injection type both vapor compression module
Injection type vapour compression unit（4）Low pressure admission pipe（3）It is connected, injection type vapour compression unit（4）Driving steam inlet
Mouth is provided with driving steam and enters steam control valve（2）, injection type vapour compression unit（4）Gland steam exhauster（5）With negative pressure steam condensing
Device-fresh air preheating device（6）Air intake be connected, negative pressure steam condenser-fresh air preheating device（6）Delivery port and solidifying water pot（7）
Water inlet be connected, coagulate water pot（7）The on-condensible gas exhaust outlet and vacuum pumping pump on top（8）Air inlet be connected, vacuum pumping pump
（8）Exhaust outlet communicated with surrounding air, coagulate water pot（7）The delivery port and condensate pump of bottom（9）Water inlet be connected, condense
Water pump（9）Delivery port and condensate postpositive disposal reuse module（10）Water inlet be connected, condensate postpositive disposal reuse mould
Block（10）Delivery port communicate and be connected with technique moisturizing, negative pressure steam condenser-fresh air preheating device（6）Inlet side and outdoor it is empty
Gas phase is led to, and air side is connected with original steam air heater or conduction oil air heater.
2. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
In described process flow, it is by existing conventional flowsheet：Extraction process add water AA+ material<1：9>——》Point
From ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》It is heavy that newborn acid adding carries out acid ---》
It is separated into curdled milk+beans stripping water（Sampling water）——》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization（130~150
℃）——》Flash distillation, cooling（65~75 DEG C）——》Spray drying ---》Albumen powder discharges, wherein the air intake being spray-dried adds
Thermal process flow is：Outdoor fresh air ---》Steam heater or hotline heater ---》Drying tower；It is adjusted to new process flow
Journey, wherein the part changed is：Flash distillation, cooling in existing common process（65~75 DEG C）Indirect steam afterwards；And a part
High drive steam ---》Injection type vapour compression unit（4）——》Negative pressure steam condenser-fresh air preheating device（6）——》
Solidifying water pot（7）——》Condensate feeding condensate postpositive disposal reuse module after separation（16）——》Extraction process adds water AA
With（Or）Add water BB；The air intake heating technological process being wherein spray-dried is adjusted to：Outdoor fresh air ---》Negative pressure steam condensing
Device-fresh air preheating device（6）——》Steam heater or hotline heater ---》Drying tower.
3. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
In described injection type vapour compression unit（4）Using negative pressure steam type injection pump configuration.
4. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
Enter steam control valve in described driving steam（2）Using motorized adjustment valve arrangement.
5. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
In described negative pressure steam condenser-fresh air preheating device（6）It is vertically arranged using heat-exchanging tube bundle.
6. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
In described negative pressure steam condenser-fresh air preheating device（6）Using heat-exchanging tube bundle lateral arrangement.
7. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
In described negative pressure steam condenser-fresh air preheating device（6）Using pressure-bearing type or longitudinal water and on-condensible gas isolating construction.
8. the vegetable protein flash-off steam reuse method as claimed in claim 1 based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology, its feature exists
, also can split in the part included by described negative pressure steam condenser-fresh air preheating module and pipeline composition integral structure
Formula is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710345023.XA CN107188925A (en) | 2017-05-16 | 2017-05-16 | A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology |
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|---|---|---|---|
| CN201710345023.XA CN107188925A (en) | 2017-05-16 | 2017-05-16 | A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology |
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| CN107188925A true CN107188925A (en) | 2017-09-22 |
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| CN201710345023.XA Pending CN107188925A (en) | 2017-05-16 | 2017-05-16 | A kind of vegetable protein flash-off steam reuse method based on HEAT PUMP BASED ON EJECTING PRINCIPLE technology |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110966788A (en) * | 2019-12-24 | 2020-04-07 | 山东省科学院能源研究所 | Waste heat utilization method of waste heat upgrading system based on hydraulic jet |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110966788A (en) * | 2019-12-24 | 2020-04-07 | 山东省科学院能源研究所 | Waste heat utilization method of waste heat upgrading system based on hydraulic jet |
| CN110966788B (en) * | 2019-12-24 | 2021-07-20 | 山东省科学院能源研究所 | Waste heat utilization method of waste heat upgrading system based on hydraulic jet |
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