CN204193536U - A kind of high-efficiency multi-section preheating plate-type evaporator - Google Patents
A kind of high-efficiency multi-section preheating plate-type evaporator Download PDFInfo
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- CN204193536U CN204193536U CN201420630729.2U CN201420630729U CN204193536U CN 204193536 U CN204193536 U CN 204193536U CN 201420630729 U CN201420630729 U CN 201420630729U CN 204193536 U CN204193536 U CN 204193536U
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Abstract
The utility model discloses a kind of high-efficiency multi-section preheating plate-type evaporator, comprise the first plate bundle and the second plate bundle that are stacked together, first plate is intrafascicular comprises multiple the first plate alternately and the second plate, and the second plate is intrafascicular comprises multiple the 3rd plate alternately and the 4th plate; First plate bundle comprises material preheating system, and the second plate bundle comprises evaporative condenser system, is provided with dividing plate between the first plate bundle and the second plate bundle, dividing plate offers the opening be connected with preheating saturated vapor passage and preheating saturated vapor passing away.Plate type preheater and plate-type evaporator unite two into one by the utility model, have saved equipment one-time investment expense, have saved space, improve the treating capacity of unit interval.
Description
Technical field
The utility model belongs to heat exchanger technology field, is specifically related to a kind of high-efficiency multi-section preheating plate-type evaporator.
Background technology
High-efficiency multi-section preheating plate-type evaporator is as the preheating evaporation concentration equipment of a kind of advanced person, be mainly used in material preheating and make the moisture in rare material, by the transmission of steam high temperature enthalpy, moisture is evaporated, thus obtain concentrated material, and be widely used in chemistry and pharmaceuticals industry, such as organic acid, the purification of amine and alcohol etc.Be applied in Food & Drink industry, concentrating of such as dairy products, fruit juice, sugar etc.Also natural organic products industry is applied to, such as fermentation industry, the evaporation of glue, thickness water etc.Also be applied to the Heisui River evaporation in paper-making industry and concentrate.Along with modernization of industry technology development, plate-type evaporator application will be more and more extensive.
Current plate-type evaporator, arranges external preheater to reach the pre-heat effect to material medium usually.As application number is: 201120222530.2, utility model name is called: a kind of patent of high dense organic and/or inorganic wastewater Zero discharging system, this system comprises buffering regulating reservoir, mechanical steam recompression vapo(u)rization system, distillate treatment system and equipment for separating liquid from solid, buffering regulating reservoir, mechanical steam recompression vapo(u)rization system and distillate treatment system connect successively, equipment for separating liquid from solid and mechanical steam recompression vapo(u)rization system and cushion regulating reservoir and be connected; Mechanical steam recompression vapo(u)rization system comprises preheater, evaporimeter, separator and compressor.In its waste water treatment process, waste water enters mechanical steam recompression evaporation system, waste water enters preheater by water pump, after preheater preheats, temperature reaches or close to evaporating temperature, waste water after preheating enters evaporimeter through evaporator waterwater entrance, absorb heat, major part liquid is evaporated, liquid-vapor mixture leaves evaporimeter through the outlet of evaporator liquid-vapor mixture, enter separator through separator inlet and carry out vapor-liquid separation, take on-condensible gas away by vavuum pump regulating system vacuum, water vapour after separation enters compressor through separator vapor outlet, compressor consumes electric energy and does work to it, increase the temperature and pressure of steam, the steam of Pressurized-heated gets back to evaporimeter through evaporimeter steam inlet, heat exchange is carried out with material, heat release forms the good distillate of water quality, distillate is got back to preheater through the outlet of evaporimeter distillate and is heated raw material, distillate treatment system is entered through the outlet of preheater distillate after distillate heat exchange cooling, the concentrate of the high pollution thing in separator enters equipment for separating liquid from solid through separator concentrated solution outlet by water pump.The climbing-film evaporation apparatus of this external preheater, thermal loss is comparatively large, and heat transfer efficiency is low, and technique adjunct processes is more complicated, and floor space is also larger.
Utility model content
Technical problem to be solved in the utility model is for above-mentioned the deficiencies in the prior art, a kind of high-efficiency multi-section preheating plate-type evaporator is provided, plate type preheater and plate-type evaporator unite two into one by the utility model, save equipment one-time investment expense, save space, improve the treating capacity of unit interval.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is, a kind of high-efficiency multi-section preheating plate-type evaporator, comprises the first plate bundle and the second plate bundle that are stacked together, first plate bundle is used for not concentrating preheating of material, and the second plate bundle is used for the evaporation and concentration of material; First plate is intrafascicular comprises multiple the first plate alternately and the second plate, and the second plate is intrafascicular comprises multiple the 3rd plate alternately and the 4th plate; First plate bundle comprises material preheating system, material preheating system comprises fluid mechanics passing away, preheating saturated vapor admission passage, preheating saturated vapor passing away and condensed water after not concentrated fluid mechanics admission passage, preheating and on-condensible gas passage, and each passage is by the opening composition being arranged on same position on each plate; Second plate bundle comprises evaporative condenser system, evaporative condenser system comprises fluid mechanics admission passage, concentrate and indirect steam passing away after preheating, saturated vapor admission passage and condensed water and on-condensible gas passing away, second plate bundle also comprises preheating saturated vapor passage, and each passage is made up of the opening being arranged on same position on each plate; Be provided with dividing plate between first plate bundle and the second plate bundle, dividing plate offer the opening be connected with preheating saturated vapor passage and preheating saturated vapor passing away;
First plate is provided with first passage spacer assembly, first passage spacer assembly makes to form the first preheating material runner between adjacent two plates, and the fluid mechanics passing away after not concentrating fluid mechanics admission passage, multiple first preheating material runner and preheating is connected, and make preheating saturated vapor admission passage, preheating saturated vapor passing away and condensed water and on-condensible gas passage independently of one another, and all separate with the first preheating material runner; Second plate is provided with second channel spacer assembly, second channel spacer assembly makes to form the first Preheated steam runner between adjacent two plates, and preheating saturated vapor admission passage, multiple the first Preheated steam runner arranged side by side and condensed water and on-condensible gas passage are connected successively, and it is independent of one another to make not concentrate fluid mechanics admission passage, preheating saturated vapor passing away and fluid mechanics passing away, and all isolated with the first Preheated steam runner; Preheating saturated vapor passing away is connected by exterior line and preheating saturated vapor admission passage, and the other end of preheating saturated vapor admission passage is connected by multiple preheating saturated vapor runner arranged side by side and condensed water and on-condensible gas passage; After fluid mechanics passing away after preheating and preheating, fluid mechanics admission passage is connected by exterior line; 3rd plate is provided with third channel spacer assembly, third channel spacer assembly makes to form steam flow channel between adjacent two plates, and make saturated vapor admission passage, multiple steam flow channel and condensed water and on-condensible gas passing away UNICOM successively, and after making concentrate and indirect steam passing away, preheating saturated vapor passage and preheating, fluid mechanics admission passage is independent of one another, and all separate with steam flow channel; 4th plate is provided with four-way spacer assembly, four-way spacer assembly makes to form material flow path between adjacent two plates, and fluid mechanics admission passage UNICOM successively after making concentrate and indirect steam passing away, material flow path and preheating, and make saturated vapor admission passage, preheating saturated vapor passage and condensed water and on-condensible gas passing away independently of one another, and all separate with material flow path.
Further, the number of the fluid mechanics passing away after the preheating that this first plate is intrafascicular is one or two, and the number of other each passages is two.
Further, this first passage spacer assembly comprises the first draw-in groove be arranged on the first plate, the first sealing gasket matched with the first plate is provided with in first draw-in groove, second channel spacer assembly comprises the second draw-in groove be arranged on the second plate, be provided with the second sealing gasket matched with the second plate in second draw-in groove, the concaveconvex structure that the first draw-in groove and the second draw-in groove are suppressed by its both sides surrounds.
Further, this third channel spacer assembly comprises the 3rd draw-in groove be arranged on the 3rd plate, is provided with the 3rd sealing gasket matched with the 3rd plate in the 3rd draw-in groove; Four-way spacer assembly comprises the 4th draw-in groove be arranged on the 4th plate, is provided with the 4th sealing gasket matched with the 4th plate in the 4th draw-in groove, and the concaveconvex structure that the 3rd draw-in groove and the 4th draw-in groove are suppressed by its both sides surrounds.
Further, the both sides in the middle part of this each plate are provided with stress hole.
Further, the upper end edge horizontal direction of this first plate and the second plate is provided with the not concentrated fluid mechanics import of the first not concentrated fluid mechanics import and second, the side of the first plate and the second plate vertically offers the first preheating saturated vapor inlet port and the first preheating saturated vapor outlet, the opposite side of the first plate and the second plate vertically offers the second preheating saturated vapor inlet port and the second preheating saturated vapor outlet, the base angle place, left and right, lower end of the first plate and the second plate offers the first condensed water and on-condensible gas outlet and the second condensed water and on-condensible gas outlet, the bottom of the first plate and the second plate offers the fluid mechanics outlet after preheating, each opening is all arranged at sheet edges place, the upper end edge horizontal direction of the 3rd plate and the 4th plate is provided with the first concentrate and indirect steam outlet and the second concentrate and indirect steam and exports, the side of the 3rd plate and the 4th plate vertically offers the 3rd saturated vapor inlet port and the first preheating saturated vapor import, the opposite side of the 3rd plate and the 4th plate vertically offers the 4th saturated vapor inlet port and the second preheating saturated vapor import, the base angle place, left and right, lower end of the 3rd plate and the 4th plate offers the 3rd condensed water and on-condensible gas outlet and the 4th condensed water and on-condensible gas outlet, the bottom of the 3rd plate and the 4th plate to offer after the first preheating fluid mechanics inlet port after fluid mechanics inlet port and the second preheating in the horizontal direction, each opening is all arranged on sheet edges place.
Further, this each plate is buckplate structure or corrugated board structures.
Further, this each plate is rectangle, and the opening shape of each condensed water and on-condensible gas outlet be square, and this foursquare angle is fillet, and the shape of other each opening is rectangle.
Further, this each stress hole is positioned on the horizontal axis of plate, and is all arranged on sheet edges place, and each stress hole is uncovered shape outside plate.
Further, this the first plate bundle and the second plate bundle are arranged between movable strong plate and fixing strong plate, and be fixedly connected with by clamp stud, one end of first plate bundle is connected with the strong plate of activity, the other end of the second plate bundle is connected with fixing strong plate, be provided with dividing plate between first plate bundle and the second plate bundle, the upper end of the intrafascicular plate of each plate all to be hung with the top guide bar of framework by suppending hole and is connected; The lower end of the intrafascicular plate of each plate is all connected with the lower guide rod of framework by locating hole.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, tool has the following advantages: 1. plate type preheater and plate-type evaporator are united two into one, effectively can reduce the thermal loss in traditional external preheater connection evaporimeter process, material and steam is made to be reached by heat exchange fast or close to evaporating temperature, and common part saturated vapor, save saturated vapor resource, reduce financial cost.On the other hand, this cramped construction preheater and evaporimeter are incorporated in an equipment, significantly can reduce floor space, be more suitable for the engineering that occupation area of equipment requirement is less, equipment one-time investment expense can be saved like this, also save simultaneously and take up an area space, and save construction investment.2. each plate bundle of evaporimeter is provided with two-way steam channel and material admission passage, adds the treating capacity of saturated vapor flow and not concentrated material in the unit interval, improves production efficiency, save the energy.3. in evaporimeter, the opening on each plate is all arranged on edge, increases effective heat transfer area, and because each opening is round effective heat-transfer area, can effectively utilize heat, improves evaporative condenser efficiency.4. the both sides at the middle part of each plate offer stress hole, and plate both sides arrange the mode of stress hole, make stress hole nearest from two ends plate draw-in groove, make sealing gasket better tightness, make pressure of equipment ability stronger.5. in equipment, each plate bundle to hang on top guide bar and to be located, and plate bundle can move freely on top guide bar, is convenient to check, dismounting and change plate, the also each plate of convenient cleaning.
Accompanying drawing explanation
Fig. 1 is the structural representation of the first plate bundle in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 2 is the structural representation of the second plate bundle in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 3 is the structural representation of the first plate in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 4 is the structural representation of the second plate in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 5 is the structural representation of the 3rd plate in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 6 is the structural representation of the 4th plate in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 7 is the structural representation of a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Fig. 8 is a kind of high-efficiency multi-section preheating of the utility model board-like vaporizer side view (fixing strong plate end).
Fig. 9 is the board-like vaporizer side view of a kind of high-efficiency multi-section preheating of the utility model (movable strong plate end).
Figure 10 a is the first plate and the rear a-a profile of the second plate combination in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Figure 10 b is the first plate and the rear b-b profile of the second plate combination in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Figure 11 a is the 3rd plate and the rear a-a profile of the 4th plate combination in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Figure 11 b is the 3rd plate and the rear b-b profile of the 4th plate combination in a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator.
Figure 12 a is the part that the board-like evaporator evaporation of a kind of high-efficiency multi-section of the utility model preheating concentrates the flow chart of fluid mechanics.
Figure 12 b is another part that the board-like evaporator evaporation of a kind of high-efficiency multi-section of the utility model preheating concentrates the flow chart of fluid mechanics.(Figure 12 a and Figure 12 b constitutes the flow chart that the board-like evaporator evaporation of a kind of high-efficiency multi-section of the utility model preheating concentrates fluid mechanics jointly).
Detailed description of the invention
Embodiment
As depicted in figs. 1 and 2, a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, comprise the first plate bundle 1 of being stacked together and the second plate bundle 2, first plate bundle 1 preheating for not concentrated material, the second plate bundle 2 is for the evaporation and concentration of material; First plate bundle 1 comprises multiple the first plate A alternately and the second plate B, and the second plate bundle 2 comprises multiple the 3rd plate C alternately and the 4th plate D; First plate bundle 1 comprises material preheating system, material preheating system comprises the fluid mechanics passing away m after not concentrated fluid mechanics admission passage f, preheating, preheating saturated vapor admission passage g, preheating saturated vapor passing away h and condensed water and on-condensible gas passage n, and each passage is by the opening composition being arranged on same position on each plate; Second plate bundle 2 comprises evaporative condenser system, evaporative condenser system comprises fluid mechanics admission passage d after preheating, concentrate and indirect steam passing away a, saturated vapor admission passage b and condensed water and on-condensible gas passing away e, second plate bundle 2 also comprises preheating saturated vapor passage c, and each passage is made up of the opening being arranged on same position on each plate.The number of the fluid mechanics passing away m after the preheating in the first plate bundle 1 is one or two, and the number of other each passages is two.Be provided with dividing plate 7 between first plate bundle 1 and the second plate bundle 2, dividing plate 7 offer the opening be connected with preheating saturated vapor passage c and preheating saturated vapor passing away h.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, first plate A is provided with first passage spacer assembly, first passage spacer assembly makes to form the first preheating material runner between adjacent two plates, and the fluid mechanics passing away m after not concentrating fluid mechanics admission passage f, multiple first preheating material runner and preheating is connected, and make preheating saturated vapor admission passage g, preheating saturated vapor passing away h and condensed water and on-condensible gas passage n independently of one another, and all separate with the first preheating material runner; Second plate B is provided with second channel spacer assembly, second channel spacer assembly makes to form the first Preheated steam runner between adjacent two plates, and preheating saturated vapor admission passage g, multiple thing first Preheated steam runner arranged side by side and condensed water and on-condensible gas passage n are connected successively, and it is independent of one another to make not concentrate fluid mechanics admission passage f, preheating saturated vapor passing away h and fluid mechanics passing away m, and all isolated with the first Preheated steam runner; Preheating saturated vapor passing away h is connected with preheating saturated vapor admission passage g by exterior line 14, and the other end of preheating saturated vapor admission passage g is connected by multiple preheating saturated vapor runner arranged side by side and condensed water and on-condensible gas passage n; After fluid mechanics passing away m after preheating and preheating, fluid mechanics admission passage d is connected by exterior line; As shown in Figure 3 and Figure 4, first passage spacer assembly comprises the first draw-in groove 1-10 be arranged on the first plate A, the the first sealing gasket 1-10-1 matched with the first plate A is provided with in first draw-in groove 1-10, second channel spacer assembly comprises the second draw-in groove 1-10a be arranged on the second plate B, be provided with the second sealing gasket 1-10a-2 matched with the second plate B in second draw-in groove 1-10a, the concaveconvex structure that the first draw-in groove 1-10 and the second draw-in groove 1-10a suppresses by its both sides surrounds.
As shown in Figure 5 and Figure 6, a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, 3rd plate C is provided with third channel spacer assembly, third channel spacer assembly makes to form steam flow channel between adjacent two plates, and make saturated vapor admission passage b, multiple steam flow channel and condensed water and on-condensible gas passing away e UNICOM successively, and after making concentrate and indirect steam passing away a, preheating saturated vapor passage c and preheating, fluid mechanics admission passage d is independent of one another, and all separate with steam flow channel; 4th plate D is provided with four-way spacer assembly, four-way spacer assembly makes to form material flow path between adjacent two plates, and fluid mechanics admission passage d UNICOM successively after making concentrate and indirect steam passing away a, material flow path and preheating, and make saturated vapor admission passage b, preheating saturated vapor passage c and condensed water and on-condensible gas passing away e independently of one another, and all separate with material flow path.Third channel spacer assembly comprises the 3rd draw-in groove 2-11 be arranged on the 3rd plate C, is provided with the 3rd sealing gasket 2-11-1 matched with the 3rd plate C in the 3rd draw-in groove 2-11; Four-way spacer assembly comprises the 4th draw-in groove 2-11d be arranged on the 4th plate C, be provided with the 4th sealing gasket 2-11d-2 matched with the 4th plate D in 4th draw-in groove 2-11d, the concaveconvex structure that the 3rd draw-in groove 2-11 and the 4th draw-in groove 2-11d suppresses by its both sides surrounds.
Both sides in the middle part of each plate are provided with stress hole, and stress hole is positioned on the horizontal axis of plate, and the stress hole of each is all arranged on sheet edges place, and each stress hole is uncovered shape outside plate.The both sides of the first plate A and the second plate B are respectively arranged with the first stress hole 1-12 and the second stress hole 1-13, and the both sides on the 3rd plate C and the 4th plate D are respectively arranged with the 3rd stress hole 2-12 and the 4th stress hole 2-13,
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, the upper end edge horizontal direction of the first plate A and the second plate B is provided with the not concentrated fluid mechanics import 1-2 of the first not concentrated fluid mechanics import 1-1 and second, the side of the first plate A and the second plate B vertically offers the first preheating saturated vapor inlet port 1-3 and the first preheating saturated vapor outlet 1-5, the opposite side of the first plate A and the second plate B vertically offers the second preheating saturated vapor inlet port 1-4 and the second preheating saturated vapor outlet 1-6, the base angle place, left and right, lower end of the first plate A and the second plate B offers the first condensed water and on-condensible gas outlet 1-7 and the second condensed water and on-condensible gas outlet 1-8, the bottom of the first plate A and the second plate B offers the fluid mechanics outlet 1-9 after preheating, each opening is all arranged at sheet edges place, the upper end edge horizontal direction of the 3rd plate C and the 4th plate D is provided with the first concentrate and indirect steam outlet 2-1 and the second concentrate and indirect steam outlet 2-2, the side of the 3rd plate C and the 4th plate D vertically offers the 3rd saturated vapor inlet port 2-3 and the first preheating saturated vapor import 2-5, the opposite side of the 3rd plate C and the 4th plate D vertically offers the 4th saturated vapor inlet port 2-4 and the second preheating saturated vapor import 2-6, the base angle place, left and right, lower end of the 3rd plate C and the 4th plate D offers the 3rd condensed water and on-condensible gas outlet 2-7 and the 4th condensed water and on-condensible gas outlet 2-8, the bottom of the 3rd plate C and the 4th plate D to offer after the first preheating fluid mechanics inlet port 2-10 after fluid mechanics inlet port 2-9 and the second preheating in the horizontal direction, each opening is all arranged on sheet edges place.Each plate is buckplate structure or corrugated board structures.Each plate is rectangle, and the opening shape of each condensed water and on-condensible gas outlet be square, and this foursquare angle is fillet, and the shape of other each opening is rectangle.
As shown in Figure 7, Figure 8 and Figure 9, a kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, first plate bundle 1 and the second plate bundle 2 are arranged between movable strong plate 10 and fixing strong plate 3, and be fixedly connected with by clamp stud 13, one end of first plate bundle 1 is connected with the strong plate 10 of activity, the other end of the second plate bundle 2 is connected with fixing strong plate 3, be provided with dividing plate 7 between first plate bundle 1 and the second plate bundle 2, the upper end of the intrafascicular plate of each plate all to be hung with the top guide bar 12 of framework by suppending hole and is connected; The lower end of the intrafascicular plate of each plate is all connected with the lower guide rod 15 of framework by locating hole.Opening on fixing strong plate 3 is consistent with the aperture position of each plate in the second plate bundle 2, and the opening on movable strong plate 10 is consistent with the aperture position on each plate in the first plate bundle 1.Each plate in first plate bundle 1 being the first suppending hole 1-14 and the first locating hole 1-15, each plate in the second plate bundle 2 is the second suppending hole 2-14 and the second locating hole 2-15.
As as-shown-in figures 10 a and 10b, after first plate A and the second plate B combines, multiple contact is formed between adjacent plate, owing to forming these a large amount of contact supporting plate bodies, plate rigidity is improved, be enough to bear very high interior pressure, simultaneously because all multiconductors support mutually, formed runner can make steam and fluid mechanics alternately through.Buckplate is typical netted stream plate, fluid mechanics is netted flowing along plate face, and the size and Orientation of speed constantly changes, and thus evokes and enhances the strong turbulence of liquid, can obtain high heat transfer efficiency under lower flow velocity, corresponding fluid resistance is also less.Preheating material fluid 3. and steam 1. flow in runner between adjacent panels.And in all multiple flow passages of the first plate A and the second plate B combination, if the second plate B and the first plate A is combined into runner, and enter and be preheated fluid mechanics 3., 1. the runner that so its adjacent first plate A and the second plate B is combined into must walk steam, can make steam 1. be preheated fluid mechanics and 3. in staggered runner, carry out heat exchange, thus make fluid mechanics preheating, and to reach or close to the object of evaporating temperature.As shown in Figure 11 a and Figure 11 b, after 3rd plate C and the 4th plate D combines, multiple contact is formed between adjacent plate, owing to forming these a large amount of contact supporting plate bodies, plate rigidity is improved, be enough to bear very high interior pressure, simultaneously because all multiconductors support mutually, formed runner can make steam and fluid mechanics alternately through.Buckplate is typical netted stream plate, fluid mechanics is netted flowing along plate face, and the size and Orientation of speed constantly changes, and thus evokes and enhances the strong turbulence of liquid, can obtain high heat transfer efficiency under lower flow velocity, corresponding fluid resistance is also less.Concentrated fluid mechanics 5. and steam 1. flow in runner between adjacent panels.And in all multiple flow passages combined at the 3rd plate C and the 4th plate D, if the 3rd plate C and the 4th plate D is combined into runner, and enter not concentrated fluid mechanics 5., 1. the runner be so combined between its adjacent 4th plate D and the 3rd plate C must walk steam, steam can be made 1. 5. in staggered runner, to carry out heat exchange with not concentrated fluid mechanics, thus reach the object of fluid mechanics evaporation and concentration.
As depicted in figs. 12 a and 12b, jointly constitute the board-like evaporator operation flowchart process figure of a kind of high-efficiency multi-section preheating of the utility model, the heat exchanging process steam that to be fresh saturated vapor lead to preheating section respectively by total jet chimney 1. and the steam leading to climbing-film evaporation section 1., come to heat preheating section flow process and climbing-film evaporation section flow process respectively.In preheating section flow process, 1. fresh saturated vapor divides two to flowing to both sides saturated vapor linked hole c below climbing-film evaporation section second plate bundle 2, and enter both sides saturated vapor cross over pipe h below material preheating section first plate bundle 1 through two STHs below central dividing plate 7, until below movable strong plate both sides steam (vapor) outlet is out, from bottom to top 1. steam transmitted by steam exterior line 14 again and be input to both sides preheating section steam inlet above movable strong plate, and enter material preheating section plate bundle 1 vapor communication pipe g, and be dispensed in several saturated vapor runners of both sides at interval of a material preheating side runner, until the plate 8 of band blind hole.And meanwhile, saturated vapor in cross over pipe g then flows through heat transfer plate face along the saturated vapor runner of several parallel connections, saturated vapor is from top to bottom progressively condensation along plate face, condensed water is formed 2. along some steam side runner bottoms in runner, collect and enter both sides condensed water and on-condensible gas cross over pipe n, and by being incorporated to both sides condensed water and on-condensible gas communicating pipe total condensed water and on-condensible gas pipe and outside output equipment.3. the non-preheating material carrying out heat exchange with steam divides two too to flowing to into both sides non-preheating material cross over pipe f, and be dispensed in several non-preheating material side runners of both sides at interval of a steam side runner, until card plate, and meanwhile, not concentrated material in cross over pipe f, along the non-concentrate stream side runner of several parallel connections, flow through heat transfer face plate.After the non-preheating material side runner in non-preheating material mutual entry both sides, the 3. from top to bottom constantly heat exchange along plate face of non-preheating material, to form after preheating material 4. and along some fluid mechanics side runners, collect and enter material cross over pipe m after preheating, and discharge material preheating section by fluid mechanics pipe m after preheating.Then concentrated from bottom by reaching after preheating or carrying out climbing-film evaporation close to not concentrated material inlet d middle bottom mass transport after the preheating of evaporating temperature to climbing-film evaporation section by external connecting pipe road.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, in climbing-film evaporation flow process, 1. fresh saturated vapor divides two to flowing to both sides saturated vapor linked hole b above climbing-film evaporation section second plate bundle 2, and be dispensed to several saturated vapor runners of both sides at interval of not concentrated material side runner, until rear end card (plate upper part opening), and meanwhile, the saturated vapor in cross over pipe b then flows through heat transfer plate face along the saturated vapor runner of several parallel connections.After the steam flow channel of saturated vapor mutual entry both sides, saturated vapor is from top to bottom progressively condensation along plate face, condensed water is formed 2. along some steam side runner bottoms in runner, collect and enter both sides condensed water and on-condensible gas cross over pipe e, and be incorporated to total condensed water and on-condensible gas cross over pipe by both sides condensed water and on-condensible gas cross over pipe e and outside output equipment.5. not concentrated material after carrying out the preheating of heat exchange with steam divides two too to flowing to into the not concentrated material channel d in both sides, and be dispensed in several not concentrated material side runners of both sides at interval of a steam side runner, until card, and meanwhile, not concentrated material in cross over pipe d, non-concentrate stream side runner along several parallel connections flows through heat transfer face plate, 5. not concentrated material from bottom to top constantly evaporates along plate face, the concentrated material of formation and indirect steam are 6., and along some fluid mechanics side runners, collect and enter lateral condensation liquid and indirect steam passing away a, and flowed out by lateral condensation material and indirect steam cross over pipe and be incorporated to house steward and outside output equipment.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, achieve material not only preheating but also the multi-stage operation process structure evaporated in evaporimeter, unite two into one by plate type preheater and plate-type climbing film evaporator, separated by central dividing plate, high-efficiency multi-section preheating plate-type evaporator divides two sections of operations, first paragraph material preheating section is made up of the first plate bundle 1, and second segment climbing-film evaporation section is made up of the second plate bundle 2.Shared saturated vapor is thermal source, to reach material preheating and to evaporate the heat exchange effect carried out simultaneously.The beneficial effect of this process structure effectively can reduce traditional external preheater to connect thermal loss in evaporimeter process, makes material and steam be reached by heat exchange fast or close to evaporating temperature, and save live steam resource, reduction financial cost.On the other hand, this cramped construction preheater and evaporimeter are incorporated in an equipment, significantly can reduce floor space, be more suitable for the engineering that occupation area of equipment requirement is less, equipment one-time investment expense can be saved like this, also save occupation of land space is that shell-and-tube evaporator takes up an area 1/4 of space simultaneously, thus saves construction investment.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, each plate is intrafascicular comprises multiple plate, plate profile is rectangle, each plate all adopts 0.7mm-1.5mm metal sheet to be formed by casted die mould compacting, in effective heat exchange area, suppress the half billiard table shape concaveconvex structure that shape is identical, these concaveconvex structures are that 12mm-32mm half billiard table shape structural detail forms by the diameter that many projections are recessed, these billiard table shape structural details, with equilateral triangle arrangement, between billiard table shape structural detail, centre distance 20mm-42mm is greater than ball platform diameter.Ball platform shape relief elements along the vertical center line of plate, symmetrically arranged.When such layout being to assemble, half billiard table shape structural detail of its bossing being contacted with each other and forms supporting.Negative area half billiard table shape structural detail also contacts with each other and forms supporting.Between this plate supported each other, by forming the runner of 3.5mm-14mm, steam and fluid mechanics can be made to pass through.Material is netted flowing along plate face, velocity magnitude and direction constantly change, thus the strong turbulence of material is evoked, heat transfer efficiency is improved, half billiard table shape supporting between plate in heat transfer zone is counted, and equals the concavo-convex half billiard table shape structural elements number of packages on plate, owing to forming these a large amount of supporting-points, plate rigidity is increased substantially, pressure in very high equipment can be born.The runner formed, can be applicable to well, the process of the process of fibre-bearing material and high-viscosity material and not easily blocking, the vapour phase flow resistance of corresponding steam side runner and the liquid phase flow resistance of fluid mechanics side runner also less.Because offering two non-concentrate stream body openings, treating capacity being improved greatly simultaneously, being applicable to fibre-bearing fluid mechanics, and should not block containing the process of high-viscosity material fluid.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, another design feature is, each access portal on each plate is all opened in sheet edges place, mode of offering like this is of value to fluid mechanics can not produce dead angle in the process entered and flow out plate runner, heat exchange area can be made to maximize simultaneously.The number of each passage is two, is made up of the opening be opened on each plate.In the second plate bundle 2, each plate bottom offers fluid mechanics inlet port after the preheating of two rectangles in the horizontal direction, and this structure enhances material treating capacity, the material evaporation ability of strengthening device.Two rectangle saturated vapor inlet ports are offered in both sides, plate middle and upper part, This structure increases quantity of steam, improve the thermal efficiency, shorten evaporation time, two rectangle concentrates and indirect steam outlet is offered on plate top, this structure makes concentrate and indirect steam have sufficient space to pass through, and offer the import of two rectangle preheating saturated vapors in both sides, plate middle and lower part, this structure makes the saturated vapor of preheating section by evaporator section simultaneously.Same in the first plate bundle 1, both sides, each plate middle and lower part offer two rectangle preheating saturated vapor outlets, and this structure can make preheating saturated vapor pass through preheating section.Two rectangle preheating saturated vapor inlet ports are offered in both sides, plate middle and upper part, This structure increases quantity of steam, improve the pre-thermal efficiency, shorten preheating time, two rectangle non-preheating material ingate structures are symmetrical arranged to strengthen material treating capacity along the vertical center line of plate equally, the material warm-up ability of strengthening device on plate top.Such opening design, makes the treating capacity in the unit interval be greatly improved.Simultaneously in the first plate bundle 1 and the second plate bundle 2, each plate all offers steam condensate (SC) and on-condensible gas corner apertures structure, so that more condensed water and on-condensible gas are discharged.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, wherein in plate, bilateral symmetry arranges the mode of stress hole.Namely the first stress hole 1-12 on the first plate A and the second plate B and the second stress hole 1-13 is opened in, be opened in the 3rd stress hole 2-12 on the 3rd plate C and the 4th plate D and the 4th stress hole 2-13, this plate both sides arrange the mode of stress hole, beneficial effect is that stress hole is nearest from two ends plate gasket slot, after compressing plate bundle by fishbolt, can more effectively seal exchange media and can not reveal, equipment is greatly improved in safe operation, also makes pressure of equipment ability improve simultaneously.
A kind of high-efficiency multi-section preheating of the utility model plate-type evaporator, the draw-in groove on plate can suppress multiple flexible member supporting mass with swaging mould, forms building enclosure.Runner plate spacing is determined by the thickness of plate contact and rubber gasket.Be pressed with seal groove in plate surrounding, rubber gasket is used as sealing on the one hand, prevents material medium from revealing.On the other hand make it between two plates, form certain interval, as steam and fluid mechanics passage and form heat exchange.
Claims (10)
1. a high-efficiency multi-section preheating plate-type evaporator, it is characterized in that, comprise the first plate bundle (1) and the second plate bundle (2) that are stacked together, described first plate bundle (1) is not for concentrating preheating of material, and described second plate bundle (2) is for the evaporation and concentration of material; Described first plate bundle (1) comprises multiple the first plate (A) alternately and the second plate (B), and described second plate bundle (2) comprises multiple the 3rd plate (C) alternately and the 4th plate (D);
Described first plate bundle (1) comprises material preheating system, described material preheating system comprises fluid mechanics passing away (m) after not concentrated fluid mechanics admission passage (f), preheating, preheating saturated vapor admission passage (g), preheating saturated vapor passing away (h) and condensed water and on-condensible gas passage (n), and described each passage is by the opening composition being arranged on same position on each plate; Described second plate bundle (2) comprises evaporative condenser system, described evaporative condenser system comprises fluid mechanics admission passage (d), concentrate and indirect steam passing away (a) after preheating, saturated vapor admission passage (b) and cool solidifying water and on-condensible gas passing away (e), described second plate bundle (2) also comprises preheating saturated vapor passage (c), and described each passage is made up of the opening being arranged on same position on each plate;
Be provided with dividing plate (7) between described first plate bundle (1) and the second plate bundle (2), described dividing plate (7) offer the opening be connected with preheating saturated vapor passage (c) and preheating saturated vapor passing away (h);
Described first plate (A) is provided with first passage spacer assembly, described first passage spacer assembly makes to form the first preheating material runner between adjacent two plates, and fluid mechanics passing away (m) after not concentrating fluid mechanics admission passage (f), multiple first preheating material runner and preheating is connected, and make preheating saturated vapor admission passage (g), preheating saturated vapor passing away (h) and condensed water and on-condensible gas passage (n) independently of one another, and all separate with the first preheating material runner; Described second plate (B) is provided with second channel spacer assembly, described second channel spacer assembly makes to form the first Preheated steam runner between adjacent two plates, and preheating saturated vapor admission passage (g), multiple thing first Preheated steam runner arranged side by side and condensed water and on-condensible gas passage (n) are connected successively, and it is independent of one another to make not concentrate fluid mechanics admission passage (f), preheating saturated vapor passing away (h) and fluid mechanics passing away (m), and all isolated with the first Preheated steam runner; Described preheating saturated vapor passing away (h) is connected by exterior line (14) and preheating saturated vapor admission passage (g), and the other end of described preheating saturated vapor admission passage (g) is connected by multiple preheating saturated vapor runner arranged side by side and condensed water and on-condensible gas passage (n); After fluid mechanics passing away (m) after described preheating and preheating, fluid mechanics admission passage (d) is connected by exterior line;
Described 3rd plate (C) is provided with third channel spacer assembly, described third channel spacer assembly makes to form steam flow channel between adjacent two plates, and make saturated vapor admission passage (b), multiple steam flow channel and cool solidifying water and on-condensible gas passing away (e) UNICOM successively, and after making concentrate and indirect steam passing away (a), preheating saturated vapor passage (c) and preheating, fluid mechanics admission passage (d) is independent of one another, and all separate with steam flow channel; Described 4th plate (D) is provided with four-way spacer assembly, described four-way spacer assembly makes to form material flow path between adjacent two plates, and fluid mechanics admission passage (d) UNICOM successively after making concentrate and indirect steam passing away (a), material flow path and preheating, and make saturated vapor admission passage (b), preheating saturated vapor passage (c) and cool solidifying water and on-condensible gas passing away (e) independently of one another, and all separate with material flow path.
2. according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 1, it is characterized in that, the number of fluid mechanics passing away (m) after the preheating in described first plate bundle (1) is one or two, and described in other, the number of each passage is two.
3. according to a kind of high-efficiency multi-section preheating plate-type evaporator described in claim 1 or 2, it is characterized in that, described first passage spacer assembly comprises the first draw-in groove (1-10) be arranged on the first plate (A), the first sealing gasket (1-10-1) matched with the first plate (A) is provided with in described first draw-in groove (1-10), described second channel spacer assembly comprises the second draw-in groove (1-10a) be arranged on the second plate (B), the second sealing gasket (1-10a-2) matched with the second plate (B) is provided with in described second draw-in groove (1-10a), the concaveconvex structure that described first draw-in groove (1-10) and the second draw-in groove (1-10a) are suppressed by its both sides surrounds.
4. according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 3, it is characterized in that, described third channel spacer assembly comprises the 3rd draw-in groove (2-11) be arranged on the 3rd plate (C), is provided with the 3rd sealing gasket (2-11-1) matched with the 3rd plate (C) in described 3rd draw-in groove (2-11); Described four-way spacer assembly comprises the 4th draw-in groove (2-11d) be arranged on the 4th plate (C), be provided with the 4th sealing gasket (2-11d-2) matched with the 4th plate (D) in described 4th draw-in groove (2-11d), the concaveconvex structure that described 3rd draw-in groove (2-11) and the 4th draw-in groove (2-11d) are suppressed by its both sides surrounds.
5., according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 4, it is characterized in that, the both sides in the middle part of each plate described are provided with stress hole.
6. according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 5, it is characterized in that, the upper end edge horizontal direction of described first plate (A) and the second plate (B) is provided with the not concentrated fluid mechanics import (1-2) of the first not concentrated fluid mechanics import (1-1) and second, the side of described first plate (A) and the second plate (B) vertically offers the first preheating saturated vapor inlet port (1-3) and the first preheating saturated vapor outlet (1-5), the opposite side of described first plate (A) and the second plate (B) vertically offers the second preheating saturated vapor inlet port (1-4) and the second preheating saturated vapor outlet (1-6), the base angle place, left and right, lower end of described first plate (A) and the second plate (B) offers the first condensed water and on-condensible gas outlet (1-7) and the second condensed water and on-condensible gas outlet (1-8), the bottom of described first plate (A) and the second plate (B) offers the fluid mechanics outlet (1-9) after preheating, described each opening is all arranged at sheet edges place,
The upper end edge horizontal direction of described 3rd plate (C) and the 4th plate (D) is provided with the first concentrate and indirect steam outlet (2-1) and the second concentrate and indirect steam and exports (2-2), the side of described 3rd plate (C) and the 4th plate (D) vertically offers the 3rd saturated vapor inlet port (2-3) and the first preheating saturated vapor import (2-5), the opposite side of described 3rd plate (C) and the 4th plate (D) vertically offers the 4th saturated vapor inlet port (2-4) and the second preheating saturated vapor import (2-6), the base angle place, left and right, lower end of described 3rd plate (C) and the 4th plate (D) offers the 3rd condensed water and on-condensible gas outlet (2-7) and the 4th condensed water and on-condensible gas outlet (2-8), the bottom of described 3rd plate (C) and the 4th plate (D) to offer after the first preheating fluid mechanics inlet port (2-10) after fluid mechanics inlet port (2-9) and the second preheating in the horizontal direction, described each opening is all arranged on sheet edges place.
7., according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 6, it is characterized in that, plate described in each is buckplate structure or corrugated board structures.
8. according to a kind of high-efficiency multi-section preheating plate-type evaporator described in claim 7, it is characterized in that, plate described in each is rectangle, the opening shape of condensed water described in each and on-condensible gas outlet is square, and this foursquare angle is fillet, the shape of the opening described in other each is rectangle.
9. according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 8, it is characterized in that, described stress hole is positioned on the horizontal axis of plate, and the stress hole described in each is all arranged on sheet edges place, and stress hole described in each is uncovered shape outside plate.
10. according to a kind of high-efficiency multi-section preheating plate-type evaporator according to claim 9, it is characterized in that, described first plate bundle (1) and the second plate bundle (2) are arranged between movable strong plate (10) and fixing strong plate (3), and be fixedly connected with by clamp stud (13), one end of described first plate bundle (1) is connected with the strong plate of activity (10), the other end of described second plate bundle (2) is connected with fixing strong plate (3), dividing plate (7) is provided with between described first plate bundle (1) and the second plate bundle (2), the upper end of the intrafascicular plate of plate described in each all to be hung with the top guide bar (12) of framework by suppending hole and is connected, the lower end of the intrafascicular plate of plate described in each is all connected with the lower guide rod (15) of framework by locating hole.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420630729.2U CN204193536U (en) | 2014-10-28 | 2014-10-28 | A kind of high-efficiency multi-section preheating plate-type evaporator |
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| CN201420630729.2U CN204193536U (en) | 2014-10-28 | 2014-10-28 | A kind of high-efficiency multi-section preheating plate-type evaporator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104324513A (en) * | 2014-10-28 | 2015-02-04 | 赵弘毅 | Efficient multi-section preheating plate type evaporator |
| CN111167142A (en) * | 2020-01-16 | 2020-05-19 | 南京航空航天大学 | Evaporator, heat exchange concentration device and method |
-
2014
- 2014-10-28 CN CN201420630729.2U patent/CN204193536U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104324513A (en) * | 2014-10-28 | 2015-02-04 | 赵弘毅 | Efficient multi-section preheating plate type evaporator |
| CN104324513B (en) * | 2014-10-28 | 2016-02-03 | 赵弘毅 | A kind of multistage preheating plate-type evaporator |
| CN111167142A (en) * | 2020-01-16 | 2020-05-19 | 南京航空航天大学 | Evaporator, heat exchange concentration device and method |
| CN111167142B (en) * | 2020-01-16 | 2021-06-15 | 南京航空航天大学 | Evaporator, heat exchange concentration device and method |
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