CN102516129B - Production system of urea - Google Patents
Production system of urea Download PDFInfo
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- CN102516129B CN102516129B CN2011103644859A CN201110364485A CN102516129B CN 102516129 B CN102516129 B CN 102516129B CN 2011103644859 A CN2011103644859 A CN 2011103644859A CN 201110364485 A CN201110364485 A CN 201110364485A CN 102516129 B CN102516129 B CN 102516129B
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- 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
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- 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
- Y02P20/141—Feedstock
Abstract
The invention relates to a production system of urea, which comprises a stripper which is sequentially connected with a low pressure decomposition tower, a low pressure methylamine condenser and a low pressure methylamine condenser level tank in series, and is characterized by also comprising an energy recovery system which comprises a piston power exchanger with a high pressure liquid inlet, a high pressure liquid outlet, a hydraulic oil outlet and a hydraulic oil inlet, and two ports of a hydraulic motor are respectively connected with one port of the hydraulic oil outlet and a hydraulic oil tank; the other port of the hydraulic oil tank is connected with the hydraulic oil inlet, and the hydraulic motor is also connected with a fluid coupling, a high pressure methylamine pump, a clutch and a variable frequency motor in series sequentially; and the piston power exchanger is connected between the stripper and the low pressure decomposition tower in parallel, and the high pressure methylamine pump is respectively connected with the low pressure methylamine condenser level tank and a methylamine fluid high pressure scrubber. The whole system is controlled by a PLC (Programmable Logic Controller), and the high pressure energy generated in the production process can be converted into kinetic energy, so the use of electric energy is reduced, and the production cost is reduced.
Description
Technical field
The present invention is specifically related to a kind of carbamide production system, particularly a kind of carbamide production system that the high pressure energy that produces in the production process can be recycled.
Background technology
" energy recovery " refers to used energy is transformed into by specific device the process of the energy that can continue to use.
Has a large amount of fluids that contains overbottom pressure in many technological process of productions of petrochemical industry, for these high-pressure mediums, at present be by reducing valve required low voltage value to be arrived in its decompression earlier greatly, energy is discharged the back or reenters technical process, or directly emptying.In decompression and discharging process, a large amount of overbottom pressure can be converted into heat energy dissipation in environment, causes hundreds and thousands of kilowatts potential energy to be wasted, and is for the oil, the chemical industry that are exactly highly energy-consuming originally, very unfortunate.
In today of energy growing tension, energy recovery is built a resource-conserving and environment-friendly society for China for improving existing energy utilization rate, reducing carbon emission, has great importance for social sustainable development etc.Energy recovery has good application prospects in every profession and trade, is becoming the hot subject of countries in the world primary study.
For high pressure complementary energy liquid, present modal energy reclaiming method has two classes, that is: fluid non-direct contact type and fluid direct contact type.The former conversion process of energy is: pressure energy-mechanical energy (shaft work)-pressure energy; Common typical device has three kinds of the pump of reverse type, Pei Erdun type impeller and hydraulic turbines etc.
The latter's conversion process of energy is: pressure energy-pressure energy; Common typical device has two kinds of piston-type interchanger, rotary pressure interchangers.
For chemical fertilizers production, because medium is in the situation of low discharge, high pressure mostly, if also carry out energy recovery with the hydraulic turbine unit, because specific speed of hydraulic turbine is very low, mechanical loss is often quite big, and organic efficiency generally is difficult to surpass 45%; And at present domestic hydraulic turbine system is ruled all the land by external several famous brands, and price is very high, and it is not big especially reclaiming meaning.For this part complementary energy, the best way is the method with direct contact type at present; And rotary pressure interchanger difficulty of processing is very big, successfully uses case few at present; The piston-type interchanger is as the supplementary form of hydraulic turbine, is well suited for reclaiming the complementary energy in the high-pressure low-flow liquid medium of small and medium chemical fertilizer.
Summary of the invention
The invention provides a kind of carbamide production system, purpose is to solve the prior art problem, provide a kind of and the high pressure energy that produces in the urea production process can be reclaimed and converts it into kinetic energy for the production of the production system of self using, reduced the use of electric energy in the production process, reduced production costs.
The present invention's technical scheme that adopts of dealing with problems is:
Carbamide production system includes stripping tower, and the stripping tower outlet end is in series with low pressure decomposition tower, low pressure methylamine condenser, low pressure methylamine condenser level tank successively.Also be provided with energy-recuperation system, energy-recuperation system includes piston merit interchanger, piston merit interchanger has four ports, be respectively high pressure liquid entrance, high pressure liquid outlet, hydraulic efficiency oil outlet, hydraulic efficiency oil entrance, two ports of oil motor are connected with a port of hydraulic efficiency oil outlet, hydraulic reservoir respectively, and another port of hydraulic reservoir is connected with the hydraulic efficiency oil entrance.Oil motor also is in series with fluid-flywheel clutch, high pressure first ammonia pump, clutch coupling, variable-frequency motor successively.Wherein piston merit interchanger is connected in parallel between stripping tower and the low pressure decomposition tower, and high pressure first ammonia pump goes high pressure scrubber to be connected with low pressure methylamine condenser level tank, methylamine liquid respectively.
Described piston merit interchanger includes at least one pair of piston cylinder, and each is arranged side by side on frame piston cylinder.Every pair of piston cylinder has working cylinder A cylinder, the B cylinder of two sealings, is respectively equipped with piston in A cylinder, the B cylinder, and piston is with two enclosed spaces about being divided into respectively in A cylinder, the B cylinder; The piston rod that is provided with between A cylinder, the B cylinder is connected with piston in two cylinder bodies respectively, and an end that is connected piston rod with the B cylinder at the A cylinder respectively is provided with suction valve and outlet valve; Every pair of piston cylinder also all is connected with one group of exchange system, and described exchange system is made of main valve, pilot valve, dial, sliding sash, and main valve and pilot valve are hydraulicvalve; Dial is located on the piston rod, and dial is between two contacts of sliding sash upper end; Described sliding sash is located at outside the pilot valve, pilot valve include valve body, about two spools, valve rod, the valve body two ends are airtight, valve rod links together two spools, and the valve rod two ends extend to outside the valve body; The valve rod two ends link together with the two side of sliding sash respectively, are arranged with spring at the valve rod two ends outside respectively simultaneously, and the two ends of spring link together with corresponding sliding sash sidewall and valve body termination respectively; Two spools are divided into three enclosed spaces with valve inner; The valve body upper end is provided with two port C, D, and the lower end is provided with three port E, F, G, and port E, G are the outlet of high pressure control liquid, and port F is the import of high pressure control liquid; When left spool was between port C, E, right spool was between port D, the F, and port C, F are connected, and port D, G are connected; When left spool was between port C, F, right spool was between port D, the G, and port C, E are connected, and port D, F are connected;
Main valve includes valve body, four spools, and valve rod is connected in turn four spool a, b, c, d from left to right, and these four spools are divided into five enclosed spaces with valve inner; The valve body upper end is provided with two port A, B, and the lower end is provided with two port P, O, and port P is the high pressure liquid import, and port O is low hydraulic fluid outlet; End face offers one to the inner hole of extending of valve rod from it on the valve stem part between spool a and the spool b, on the valve stem part between spool c and the spool d, offer the inner hole of extending of a phase valve rod from its lower surface, these two holes are connected with the hole that valve rod inside is provided with respectively, and three holes are connected mutually; When port A was between spool a, b, port B, P were between spool b, c, and port O is between spool c, d, and port A is connected by three communicating poress on the valve rod with port O, and port B, P are connected; When port A, P were between spool a, b, port B, O were between spool b, c, and port A, P are connected, and port B, O are connected; The port C of pilot valve is connected with the left end space of main valve by pipeline, port D is connected with the right-hand member space of main valve by pipeline, the port A of main valve and the right-hand member space of B cylinder are connected by pipeline, and port B is connected by pipeline by the left end space of pipeline and A cylinder.
Described suction valve is positioned at the upper surface of A cylinder and B cylinder, and outlet valve is positioned at the lower surface of A cylinder and B cylinder.
Described interchanger has 5 pairs of piston cylinders, and every pair of piston cylinder all is connected with one group of exchange system.
Described hydraulicvalve is guiding valve.
Beneficial effect of the present invention:
(1) system configuration is simply clear and definite, and efficient is higher relatively, can convert the high-pressure energy that produces in the production process to kinetic energy, drives the operation of high pressure first ammonia pump, satisfies the outer power supply source operation of nothing of system.
(2) system regulation is simple, and running is stable, and the mature technology of utilization is many, the reliability height.
(3) with only 2 of processing medium contact components, i.e. piston merit interchanger, piston cylinder and high pressure first ammonia pump, all the other are pure hydraulic pressure, machinery and electric-controlled parts, are subjected to the influence of medium and severe environment little, and corrosive wear is few, and the life-span is long.
(4) the piston-type merit interchanger among the present invention is coupled hydro-pump and oil motor, the part number, weight, volume etc. of machine are all greatly reduced, the weight per unit power of complete machine, unit power volume all have suitable superiority, and transmission and the exchange energy of energy are finished easily.
(5) the energy drive path is short, and the liquid flowing resistance loss is little, the hydraulic efficiency height.Liquid stream is revealed little in cylinder barrel, the volumetric efficiency height; High pressure methylamine liquid directly can pass to pressure the hydraulic efficiency oil of piston the other side by piston, is different from traditionally by electric motor, promotes the mode of plunger acting, mechanical efficiency height through shaft coupling, speed reduction unit, crank connecting link.
(6) because axial force is in a basic balance on the piston both sides, and the stressed and power that be delivered on the basis by cylinder body on the piston rod is very little, little to base and the basis influence of machine, so dynamic performance is good.
(7) can realize the omnidistance stepless speed regulation of turning round, it is convenient to shut down under normal running, overload and the guarantee condition.
Description of drawings
Fig. 1 is structural representation of the present invention;
Fig. 2 is the structural representation of energy-recuperation system;
Fig. 3 is the vertical view of piston merit interchanger;
Fig. 4 is the structural representation of piston cylinder and exchange system;
Fig. 5 is the running status one of piston merit interchanger;
Fig. 6 is the running status two of piston merit interchanger;
Fig. 7 is the running status three of piston merit interchanger.
Among the figure: 100. stripping towers, 200. low pressure decomposition towers, 300. low pressure methylamine condensers, 400. low pressure methylamine condenser level tanks; 101. pilot operated valve device, 102. pilot operated valve device, 103. pilot operated valve device, 104 pilot operated valve device, 105 pilot operated valve device;
1 '. piston merit interchanger, 2 '. high pressure liquid entrance, 3 '. high pressure liquid outlet, 4 '. hydraulic efficiency oil outlet, 5 '. hydraulic efficiency oil entrance, 6 '. oil motor, 7 '. hydraulic reservoir, 8 '. fluid-flywheel clutch, 9 '. high pressure first ammonia pump, 10 '. clutch coupling, 11 '. variable-frequency motor;
Embodiment
Below in conjunction with the drawings and specific embodiments the present invention is described in further details.
Carbamide production system as shown in Fig. 1, Fig. 2, this production system is controlled by PLC, includes stripping tower 100, and stripping tower 100 outlet ends are in series with low pressure decomposition tower 200, low pressure methylamine condenser 300, low pressure methylamine condenser level tank 400 successively.Also be provided with energy-recuperation system, energy-recuperation system includes piston merit interchanger 1 ', piston merit interchanger 1 ' has four ports, be respectively high pressure liquid entrance 2 ', high pressure liquid outlet 3 ', hydraulic efficiency oil outlet 4 ', hydraulic efficiency oil entrance 5 ', two ports of oil motor 6 ' are connected with a port of hydraulic efficiency oil outlet 4 ', hydraulic reservoir 7 ' respectively, and another port of hydraulic reservoir 7 ' is connected with hydraulic efficiency oil entrance 5 '.Oil motor 6 ' also is in series with fluid-flywheel clutch 8 ', high pressure first ammonia pump 9 ', clutch coupling 10 ', variable-frequency motor 11 ' successively.Wherein piston merit interchanger 1 ' is connected in parallel between stripping tower 100 and the low pressure decomposition tower 200, and high pressure first ammonia pump 9 ' goes the high pressure scrubber (not shown) to be connected with low pressure methylamine condenser level tank 400, methylamine liquid respectively.
Described piston merit interchanger 1 ' includes 5 pairs of piston cylinders as shown in Fig. 3, Fig. 4, these 5 pairs of piston cylinders are arranged side by side on frame.Every pair of piston cylinder has working cylinder A cylinder 1, the B cylinder 2 of two sealings, is provided with piston 3 in the A cylinder 1, is provided with piston 4 in the B cylinder 2, and piston 3 will be divided into two enclosed spaces 5,6 respectively in the A cylinder 1, and piston 4 will be divided into two enclosed spaces 7,8 respectively in the B cylinder 2.The piston rod 9 that is provided with between A cylinder 1, the B cylinder 2 is connected with piston 3,4 in two cylinder bodies respectively, and an end that is connected piston rod 9 with B cylinder 2 at A cylinder 1 is provided with suction valve 10 and outlet valve 11 respectively. Suction valve 10,10 in the present embodiment is positioned at the upper surface of A cylinder 1 and B cylinder 2, and outlet valve 11,11 is positioned at the lower surface of A cylinder 1 and B cylinder 2.
Every pair of piston cylinder also all is connected with one group of exchange system, and described exchange system is made of main valve 50, pilot valve 60, dial 12, sliding sash 13, and main valve 50 and pilot valve 60 are hydraulicvalve.Dial 12 is located on the piston rod 9, and dial 12 is about sliding sash 13 upper ends between two contacts 14,14.Described sliding sash 13 is located at outside the pilot valve 60, and pilot valve 60 includes valve body 15, two spools 16,17, valve rod 18, and valve body 15 two ends are airtight, and valve rod 18 links together two spools 16,17, and valve rod 18 two ends extend to outside the valve body 15.Valve rod 18 two ends link together with the two side of sliding sash 13 respectively, are arranged with spring 19 at valve rod 18 two ends outside respectively simultaneously, and the two ends of spring 19 link together with corresponding sliding sash 13 sidewalls and valve body 15 terminations respectively.Two spools 16,17 are divided into three enclosed spaces 34 in left, center, right, 35,36 with valve body 15 inside.Valve body 15 upper ends are provided with two port C20, D21, and the lower end is provided with three port E22, F23, G24, and port E22, G24 are the outlet of high pressure control liquid, and port F23 is the import of high pressure control liquid.When spool 16 was between port C20, E22, spool 17 was between port D21, the F23, and port C20, F23 are connected, and port D21, G24 are connected.When spool 16 was between port C20, F23, spool 17 was between port D21, the G24, and port C20, E22 are connected, and port D21, F23 are connected.
Wherein the right space 8 of the port A27 of main valve 50 and B cylinder 2 is connected by pipeline, and the left space 5 of port B28 by pipeline and A cylinder 1 is connected by pipeline.The port C20 of pilot valve 60 is connected with the left space 37 of main valve 50 by pipeline, and port D21 is connected with the right space 41 of main valve 50 by pipeline.
This production system production process is as described below:
(1) between stripping tower 100, low pressure decomposition tower 200 and energy-recuperation system, adopt to divide a process control, in order to control deenergize reclaim and the low pressure decomposition tower between liquid level and flow.
When (2) the methylamine liquid liquid pressure that comes out when stripping tower 100 reaches high warning (110%), the methylamine flow quantity that enters energy-recuperation system from stripping tower 100 remains unchanged, open big pilot operated valve device 102 simultaneously, increase the amount of liquid that methylamine liquid enters low pressure decomposition tower 200.Enter the high pressure methylamine liquid of energy-recuperation system by the energy exchange of piston merit interchanger 1 ', high pressure methylamine liquid becomes low pressure methylamine liquid, and is expelled in the high pressure scrubber from piston merit interchanger 1 '.The energy of high pressure methylamine liquid to low-pressure hydraulic oil, makes it become high-pressure and hydraulic oil by energy exchange, and drives the operation of high pressure first ammonia pump 9 ', and the variable-frequency motor 11 ' that drive high pressure first ammonia pump 9 ' this moment quits work, and has reduced the use of electric energy.
(3) when the stripping tower liquid level reaches low warning (90%), at first turn down pilot operated valve device 102 until closing, reduce the amount of liquid that enters low pressure decomposition tower 200.When liquid level is still lost control of; automatically turn down the flow control valve 101 between stripping tower 100 and energy-recuperation system; when the pressure that removes high pressure scrubber can not be maintained to normal value 90% the time; variable-frequency motor 11 ' starts; fluid-flywheel clutch 8 ' oil-feed to high pressure first ammonia pump 9 ' output and additional moment of torsion, promotes and goes the pressure of high pressure scrubber to normal value; surpass normal value 10% as this value, main motor is shut down behind fluid-flywheel clutch 8 ' the automatic draining.
(4) when stripping tower liquid level (pressure) reaches low interlocking when (30% or lower), start safety interlock system immediately, automatically it is not shown in the figures to close energy-recuperation system entrance trip valve A103(), close pilot operated valve device 101,102 simultaneously, energy-recuperation system is separated with low pressure decomposition tower 200, prevent that low pressure from scurrying into high pressure, cause security incident.
(5) when breaking down, energy-recuperation system, oil motor 6 ' and associated loop etc. cause shutting down; or when high pressure first ammonia pump 9 ' switched (namely fall pump); automatically it is not shown in the figures to close earlier energy-recuperation system entrance trip valve A103(); open big pilot operated valve device 101,102 simultaneously, avoid the liquid level of stripping tower to go up too fast.Open high pressure first ammonia pump 9 ' simultaneously and give the 10 ' oiling of fluid power clutch coupling, guarantee that high pressure first ammonia pump 9 ' goes the pressure-stabilisation of high pressure scrubber about prescribed value 16Mpa.
Describing high pressure liquid and low-pressure hydraulic oil concrete energy exchange processes in piston merit interchanger below in detail is: what wherein enter in space 5 and the cylinder B2 space 8 in the cylinder A1 is methylamine liquid, what enter in space 6 and the space 7 is hydraulic efficiency oil, low-pressure hydraulic oil enters from absorption valve 10, and outlet valve 11 is discharged behind the formation high-pressure and hydraulic oil.High pressure control liquid enters in the pilot valve body 15 from the port F23 of pilot valve 60, and discharges by port E22, G24.High pressure methylamine liquid enters in the main valve by primary-valve port P29, and discharges by port O30 after becoming low pressure methylamine liquid.The variation of liquid pressure changes realization by each spatial volume in cylinder A1, the cylinder B2, and when spatial volume became big, the liquid pressure in this space descended, otherwise liquid pressure then rises.
When dial 12 contacts with right-hand member contact 14, as shown in Figure 5, when the port A27 of main valve 50 is between spool a26, b42 at this moment, port B28, P29 are between spool b42, c43, port O30 is between spool c43, d44, port A27 is connected by three communicating poress 31,33,32 on the valve rod 45 with port O30, and port B28, P29 are connected.High pressure methylamine liquid enters in the space 39 by port P29, and enters in the space 5 of A cylinder 1 along pipeline by port B28, the low pressure methylamine liquid in the B cylinder B2 right-hand member by port A27, hole 31,33,32 and port O30 discharge.And a left side that is connected with sliding sash 13
Because left and right sides spring 19,19 itself has restoring force, restoring force is greater than piston rod 9 thrust to the right when this position, therefore to begin to promote dial 12 under the effect of spring restoring force be left that cylinder A1 direction is moved to sliding sash 13, thereby drive the motion of piston rod 9 phase A cylinders 1 direction, A cylinder 1 becomes backhaul at this moment, and B cylinder 2 becomes rise.And the valve rod 18 of pilot valve also is moved to the left along with the reactive force of spring 19, and spool 16,17 is moved to the left thereupon, as shown in Figure 6.In spool 16,17 moving process, port C20 and port F23, port D21 and port G23 are interconnected gradually.High pressure control liquid enters in the main valve left end space 37 by port F23, port C20, promoting valve body 45 moves to valve body of main valve 25 right-hand members, mobile drive four spool a26, b42, c43, d44 of valve rod 45 move right, and the high pressure control liquid in the valve body of main valve 25 right-hand member spaces 41 are discharged by pilot valve port D21, port G24.In this process, the port A27 on the main valve 60 is communicated with port O30 gradually with port P29, port B28, and high pressure methylamine liquid enters into by port P29, port A27 in the right-hand member space 8 of B cylinder 2, promotes piston rod 9 and is moved to the left.
When pilot valve core 16 finally moved between port C20, the E22, spool 17 moved between port F23, the D21, and port C20 is connected fully with port F23.When the movement of valve core of main valve until port A27, P29 between spool a26, b42, port B28, O30 are between spool b43, c43 the time, this moment, port A27 was communicated with port O30 fully with port P29, port B28.This moment, spring resetted, and piston rod is not had reactive force.Enter into high pressure methylamine liquid in the space 8 and then continue to promote piston rod 9 and move left mutually, the methylamine liquid that will become low pressure in the A cylinder space 5 extrudes by primary-valve port B28, port O30.Simultaneously, dial 12 continues to move to left under the drive of piston rod 9, and contacting the back continuation with sliding sash 13 left end contacts 14 to the right, until the restoring force of spring 19 pressure greater than piston rod 9, as shown in Figure 7, whole exchange system begins commutation, and dial 12 moves right, and its process is opposite with said process.
Have 5 pairs of piston cylinders in the piston merit interchanger in the present embodiment, when work, each direction of motion to piston cylinder all is identical, and the piston cylinder in the present embodiment is general to moving 4 pairs simultaneously, a pair of as the stock piston cylinder in addition.In fact how many piston cylinders in the interchanger has to designing according to practical situation, and its structure all is identical, just the logarithm difference of piston cylinder.
Claims (4)
1. carbamide production system, include stripping tower, the stripping tower outlet end is in series with low pressure decomposition tower, low pressure methylamine condenser, low pressure methylamine condenser level tank successively, it is characterized in that: also be provided with energy-recuperation system, energy-recuperation system includes piston merit interchanger, piston merit interchanger has four ports, be respectively high pressure liquid entrance, high pressure liquid outlet, hydraulic efficiency oil outlet, hydraulic efficiency oil entrance, two ports of oil motor are connected with a port of hydraulic efficiency oil outlet, hydraulic reservoir respectively, and another port of hydraulic reservoir is connected with the hydraulic efficiency oil entrance; Oil motor also is in series with fluid-flywheel clutch, high pressure first ammonia pump, clutch coupling, variable-frequency motor successively; Wherein piston merit interchanger is connected in parallel between stripping tower and the low pressure decomposition tower, and high pressure first ammonia pump goes high pressure scrubber to be connected with low pressure methylamine condenser level tank, methylamine liquid respectively, and total system is controlled by PLC;
Described piston merit interchanger includes at least one pair of piston cylinder, and each is arranged side by side on frame piston cylinder; Every pair of piston cylinder has working cylinder A cylinder, the B cylinder of two sealings, is respectively equipped with piston in A cylinder, the B cylinder, and piston is with two enclosed spaces about being divided into respectively in A cylinder, the B cylinder; The piston rod that is provided with between A cylinder, the B cylinder is connected with piston in two cylinder bodies respectively, and an end that is connected piston rod with the B cylinder at the A cylinder respectively is equipped with suction valve and outlet valve; Every pair of piston cylinder also all is connected with one group of exchange system, and described exchange system is made of main valve, pilot valve, dial, sliding sash, and main valve and pilot valve are hydraulicvalve; Dial is located on the piston rod, and dial is between two contacts of sliding sash upper end; Described sliding sash is located at outside the pilot valve, pilot valve include valve body, about two spools, valve rod, the valve body two ends are airtight, valve rod links together two spools, and the valve rod two ends extend to outside the valve body; The valve rod two ends link together with the two side of sliding sash respectively, are arranged with spring at the valve rod two ends outside respectively simultaneously, and the two ends of spring link together with corresponding sliding sash sidewall and valve body termination respectively; Two spools are divided into three enclosed spaces with valve inner; The valve body upper end is provided with two port C, D, and the lower end is provided with three port E, F, G, and port E, G are the outlet of high pressure control liquid, and port F is the import of high pressure control liquid; When left spool was between port C, E, right spool was between port D, the F, and port C, F are connected, and port D, G are connected; When left spool was between port C, F, right spool was between port D, the G, and port C, E are connected, and port D, F are connected;
Main valve includes valve body, four spools, and valve rod is connected in turn four spool a, b, c, d from left to right, and these four spools are divided into five enclosed spaces with valve inner; The valve body upper end is provided with two port A, B, and the lower end is provided with two port P, O, and port P is the high pressure liquid import, and port O is low hydraulic fluid outlet; End face offers one to the inner hole of extending of valve rod from it on the valve stem part between spool a and the spool b, on the valve stem part between spool c and the spool d, offer the inner hole of extending of a phase valve rod from its lower surface, these two holes are connected with the hole that valve rod inside is provided with respectively, and three holes are connected mutually; When port A was between spool a, b, port B, P were between spool b, c, and port O is between spool c, d, and port A is connected by three communicating poress on the valve rod with port O, and port B, P are connected; When port A, P were between spool a, b, port B, O were between spool b, c, and port A, P are connected, and port B, O are connected; The port C of pilot valve is connected with the left end space of main valve by pipeline, port D is connected with the right-hand member space of main valve by pipeline, the port A of main valve and the right-hand member space of B cylinder are connected by pipeline, and port B is connected by pipeline by the left end space of pipeline and A cylinder.
2. the carbamide production system described in claim 1, it is characterized in that: described suction valve is positioned at the upper surface of A cylinder and B cylinder, and outlet valve is positioned at the lower surface of A cylinder and B cylinder.
3. the carbamide production system described in claim 1 or 2, it is characterized in that: described interchanger has 5 pairs of piston cylinders, and every pair of piston cylinder all is connected with one group of exchange system.
4. the carbamide production system described in claim 3, it is characterized in that: described hydraulicvalve is guiding valve.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2011103644859A CN102516129B (en) | 2011-11-17 | 2011-11-17 | Production system of urea |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2011103644859A CN102516129B (en) | 2011-11-17 | 2011-11-17 | Production system of urea |
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| CN102516129B true CN102516129B (en) | 2013-08-07 |
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| CN104478761A (en) * | 2014-08-20 | 2015-04-01 | 江苏飞翔泵业制造有限公司 | Urea production line |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1702320A (en) * | 2005-06-17 | 2005-11-30 | 国家海洋局杭州水处理技术研究开发中心 | Double-cylinder hydraulic energy recovery device |
| DE102004050022A1 (en) * | 2004-10-13 | 2006-04-27 | L'orange Gmbh | Device for cooling a nozzle for injecting a reducing agent into an engine exhaust system comprises a cooling circuit through which the reducing agent is circulated between injections |
| CN201375831Y (en) * | 2009-04-16 | 2010-01-06 | 中国海洋石油总公司 | Ammonia condenser of urea device |
| CN201424388Y (en) * | 2009-04-16 | 2010-03-17 | 中国海洋石油总公司 | Urea process wastewater recovering device |
| CN201783322U (en) * | 2010-09-01 | 2011-04-06 | 中国海洋石油总公司 | Ammonium carbamate solution energy recovery device for CO2 stripping tower |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5412077B2 (en) * | 2008-10-01 | 2014-02-12 | キャタピラー エス エー アール エル | Power regeneration mechanism for hydraulic work machines |
-
2011
- 2011-11-17 CN CN2011103644859A patent/CN102516129B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102004050022A1 (en) * | 2004-10-13 | 2006-04-27 | L'orange Gmbh | Device for cooling a nozzle for injecting a reducing agent into an engine exhaust system comprises a cooling circuit through which the reducing agent is circulated between injections |
| CN1702320A (en) * | 2005-06-17 | 2005-11-30 | 国家海洋局杭州水处理技术研究开发中心 | Double-cylinder hydraulic energy recovery device |
| CN201375831Y (en) * | 2009-04-16 | 2010-01-06 | 中国海洋石油总公司 | Ammonia condenser of urea device |
| CN201424388Y (en) * | 2009-04-16 | 2010-03-17 | 中国海洋石油总公司 | Urea process wastewater recovering device |
| CN201783322U (en) * | 2010-09-01 | 2011-04-06 | 中国海洋石油总公司 | Ammonium carbamate solution energy recovery device for CO2 stripping tower |
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| Publication number | Publication date |
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| CN102516129A (en) | 2012-06-27 |
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