2011年12月30日星期五

Special cleaning heat exchanger

Special cleaning heat exchanger
However, the heat exchanger fouling and severe congestion, such as condensation,cooler, usually because the water contains large amounts of calcium and magnesium ions, when the water through the tube bundle heat exchanger tube surface evaporation, precipitation of calcium and magnesium deposition in the wall to form a hard scale layers, with the general approach to be ineffective, it must be such aschemical or mechanical cleaning methods.

Chemical cleaning is the use of cleaning agents and dirt layer from the chemical reaction method to remove the fouling, for more complex shape of the cleaningcomponents, such as the U-tube heat exchanger cleaning, pipe cleaning between.This cleaning method is that the metal has a slight corrosion injury. Mechanicalcleaning is the easiest blade, rotary wire brush to remove the hard dirt floor, coke or other deposits.

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Pressure vessel coated with anti-corrosion

Pressure vessel coated with anti-corrosion coatings
Pressure vessel inspection by the Quality Division personnel inspected themanufacturing quality of the coating allows the coating corrosion.

Before coating the metal surface should be kept dry, uneven and scratches on thesurface, should be used to make grinding to remove the smooth transition is not allowed to play putty.

Anti-corrosion primer paint in addition to playing selected varieties according toconstruction plans, but still need to add intermediate coating a polyurethane paint,such as the pattern of the coating anti-corrosion coatings no special requirements,the outer surface of the pressure vessel shell should be

Pressure vessel shell exterior top coat primer 2, primer dry film thickness shall be notless than 30μm, the outer surface of the container under normal circumstances still need to finish a coating, paint color should be pale. If thermal insulation of pressure vessels or not coated finish, only primer and intermediate paint.

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2011年12月29日星期四

Stainless steel reactor temperature control

Stainless steel reactor temperature control
Stainless steel reactor temperature adaptive control adaptive control system in the control process (such as chemical reaction process) the process of continuousadjustment process PID parameters to give the best control of temperature andresponse time, this process is through effective multi-faceted determination oftemperature, temperature changes and the rate of temperature change to achieve.

Stainless steel blender has a single reactor is less than satisfied with her ​​inability tochemical production requirements, then manipulate the dual mixer or external pumpforced circulation has become a growing trend in the future. Stainless steel reactor to increase the thermal insulation means, follow the progress of heat, so heat loss downto a minimum, fully integrated control waste heat or heat can be generated after the reaction, after the direction of growth will therefore.

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Pressure vessel cladding layer quality

Pressure vessel cladding layer quality
1 pressure vessel cladding layer quality when used with most surfacing weld mustcontrol the amount of overlap between 6 ~ 8mm, welding arc welding, the weldoverlap between the lap of not less than the width of the weld.
2 pressure vessel cladding layer after surfacing weld quality difference between thelevel of not more than 0.5mm, cladding layer between the surface and not allowed inthe weld bead and the substrate material between the undercut defects.
3-layer pressure vessel welding quality requirements after the transition layer and thecorrosion layer of surfacing required for UT inspection were detected between theweld and the fusion of the substrate and the solder layer height.
4 pressure vessel cladding layer after surfacing quality and timely weld spatter to clean up both sides of the impurities, there is no weld overlay surface porosity, slagand other defects.

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2011年12月28日星期三

Heat exchanger tubes stitching

Heat exchanger tubes stitching should meet the following requirements:
Heat exchanger tubes splicing, welding butt joints should be assessed. The number of specimens, size, test methods according to JB4708 requirements; aluminum, copper, titanium welded joints can be implemented by reference.

Heat exchanger tubes stitching, butt weld with a heat exchange tube, straight tube not more than one; U-shaped tube not more than two; the shortest tube length not less than 300mm; including at least 50mm of straight pipe U-bend section of the rangeshall not have WELDS.

Heat exchanger tubes splicing, the pipe end bevel should be processed by mechanical methods, should be cleaned before welding.

Heat exchanger tubes splicing, the corresponding amount of the wrong side of the wall thickness of the tubes should not exceed 10% and not more than 0.3mm, straightness deviation will not affect the smooth tube wear is limited.

Heat exchanger tubes after docking, the table should be selected steel ball diameter on the inspection of welded joints to pass the ball to the ball to pass through.

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Pressure vessel transport Tips

Pressure vessel transport
Pressure vessels and transport should be based on the specific circumstances of thepackaging design. Design should consider the following requirements:
a. smaller overall pressure vessels, skids can be fixed to the carrying vehicle or ship.
b. larger, long length of the pressure vessel, must be supported with the bracket andtighten the hoop with a confining pressure vessels in the bay, in the tension between the pressure vessel hoop and pad to be flexible material, bracket should be firmlyfixed to the carrying vehicle or ship. Weight of 1 to 10 tons of pressure vessels, can be used wooden brackets; weight> 10 tonnes nominal diameter> 3000mm container,steel bracket should be used (with the exception saddle).
c. nominal diameter ≥ 2600mm or length> 12000mm the pressure vessel, the bottom of both sides of the package should be set at a fixed plate hook. Weight ≥ 30 tons ofpressure vessels, transport should be set up on both sides of the top bracket with thelug.
d. bracket should be set to prevent the pressure vessel deformation.

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2011年12月27日星期二

Knowledge of plate heat exchanger

Knowledge of plate heat exchanger
Plate heat exchanger consists of a set of rectangular thin metal heat transfer plateform, with the frame assembly of the clamping plate on the bracket. Plate heat exchanger consists of a set of rectangular thin metal heat transfer plate form, with theframe assembly of the clamping plate on the bracket.

Plate heat exchanger plates of two adjacent edges lined pads (all made ​​of rubber orcompressed asbestos, etc.) pressed the plates are square hole, the edges of two adjacent plates lined with gasket (variety of made ​​of rubber or compressedasbestos, etc.) pressed the plates are square hole, forming a hole fluid channel, as shown. Alternately hot and cold fluid flow on both sides of the plate through the plateheat exchanger.

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Tips for Pressure vessel pressure gauge

Pressure vessel pressure gauge of the following conditions should stop using:
1. Limited only nail gauge, in the absence of pressure, the pointer can not be returned to obstructing the nail place; infinite gauge nails only, in the absence of pressure, the value of the pointer from the zero position error exceeds the allowable pressure gauge;
2. Cover glass pressure vessel rupture or dial gauge dial scale blurred;
3 pressure vessels, pressure gauge calibration seal is damaged or exceed theperiod of validity;
4 spring pressure vessel pressure gauge table loose tube leakage or pressure gauge;
5 other effects gauge accurate indication of the pressure vessel defects.

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2011年12月26日星期一

Pressure vessel safety valve installation

Pressure vessel safety valve installation requirements
1. Safety valve should be installed vertical, and should be installed in the pressure vessel vapor space above the liquid, or gas pressure vessel and connected to the pipeline to link the space.
2. Pressure vessel and safety valve connected between the pipe and fittings through-hole, the valve cross-sectional area not less than the import area.
3. Port on the pressure vessel a number of safety valves installed, then the connectionport entrance area, a number of safety valves should be at least equal to the sum ofthe import area.
4. Pressure vessel and safety valve should be installed between the intermediate cut-off valve. For packages containing flammable, toxic level of extreme, high, moderatehazard or viscous medium pressure vessel, safety valve for ease of replacement, cleaning, can be installed between the pressure vessel and safety valve stop valve,globe valve structure and pass diameter size should not prevent the normal dischargevalve. Pressure vessel during normal operation, the valve must remain open, and addseals.
5. Safety valve installation position, should be easy inspection and maintenance.

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Laboratory reactor knowledge

Laboratory reactor with a small introduction of knowledge
A small laboratory reactor placed in the room. More than one reactor in the equipment, should be separated. Each operating room shall have direct access to the outdoors or exit channel, well-ventilated place should ensure that equipment.

In the laboratory reactor installed reactor lid, the body should be to prevent the reactorvessel and reactor vessel lid sealing surface between each bump. Cover the reactorvessel at a fixed location on the kettle body carefully, tighten the main nut, must bediagonal, symmetric and gradually tighten in multiple places. Forced to be uniform,does not allow the reactor vessel cap tilted to one side, in order to achieve a good seal.

Laboratory reactor connected at the positive and negative nuts, except for the positive and negative rotating nut, two circular rotating relative to the sealing surfacemay not all parts are connected nut assembly lines should be painted oil. Needle valve sealing system line, just gently turn the needle valve, pressure tight cover, you can achieve a good seal. Hand drive action on the high-pressure magnetic rotaryreactor, check operation is flexible.

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2011年12月23日星期五

Laboratory reactor vessel material

Laboratory reactor vessel material
Laboratory reactor is currently the high temperature, high pressure chemical reactiondevice is ideal, especially for flammable, explosive, toxic chemical reaction media, and more to show its superiority.
Laboratory reactor vessel material used mainly 1cr18Ni10Ti stainless steel, andtitanium produced according to requirements of different media (TA2), Ni (Ni6) and composite steel plate, kettle structure with flat lid, convex, and with a manhole coverclosed type reactor body, reactor cover openings can be designed according to user requirements.
Laboratory reactor mediums completely sealed from the reactor body and cover body composition seal cavity, completely solved the packing seal and mechanical seal for dynamic seal caused the leak can not be overcome, so that absolutely noleaks and the reaction medium pollution.

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Tightness test pressure vessel requirements

Tightness test pressure vessel requirements
1. Tightness test pressure vessel requirements of medium to extreme toxicity, a high degree of hazard or design does not allow micro-leakage of pressure vessels, air tightness test must be carried out.
2. Tightness test pressure vessel requirements of air-tightness test after passing the test should be conducted in the hydraulic. Design requirements for the design air pressure test of pressure vessels, the need to do the leak test should be specified ondesign drawings.
3. Tightness test pressure vessel requirements of carbon steel and low alloy steelpressure vessels, gas temperature of the test should not be less than 5 ℃; other materials, pressure vessels according to the provisions of the design drawings.
4. Pressure vessels for air tightness test, safety accessories should be installedcomplete.

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2011年12月22日星期四

Low pressure steel pressure vessel problem

Low pressure steel pressure vessel problem
1 pressure vessel steel low voltage test pressure to take 1.25P and P 0.1 in both the larger value.
2. Steel pressure vessels for low pressure not by strength calculation formula to determine the wall thickness of pressure vessels (such as stability and other factorsto consider design), should increase the pressure test pressure.
3. Steel pressure vessel design low temperature (wall temperature) is greater than orequal to 200 ℃ greater than or equal to 150 ℃ steel non-ferrous metals pressure vessels, pressure test pressure P calculated as follows:
1 = PT • [σ] / [σ] t = η • P • [σ] / [σ] t
Where: P-pressure vessel design pressure, MPa (in the pressure vessel for themaximum working pressure);
PT - design temperature pressure test under pressure, MPa;
PT-test temperature pressure test under pressure, MPa;
η-pressure test the pressure coefficient (Table 5-1);
[σ] - test temperature the material allowable stress, MPa;
[σ] t - temperature of the material design allowable stress, MPa;

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Shell and tube heat exchanger fluid flow

Shell and tube heat exchanger fluid flow
Shell and tube heat exchangers work, a fluid within the tube, known as the tube,another fluid outside the tube (shell), a fluid within the tube, known as the tube,another fluid outside the tube (shell), a fluid within the tube called the shell. Control the flow of fluid from the tubes at one end the other end of time, known as a process;-tubeheat exchanger, known as the shell. Control the flow of fluid from the tubes at one endthe other end of time, known as a process;

The U-tube heat exchangers, tube-shaped fluid from the tubes at one end through the other side of a curved section of the flow, called the two-way. Two-way more than you need to board the tube body from the U-shaped tubes at one end through the other side of a curved section of the flow, called the two-way process set points to achieve the sub-partition process, commonly used is a single tube, two-way and four-way.Arrangement of sub-processes shown in Table 5-3. Shell with a single shell and double shell are two commonly used is a single shell, shell-shell sub-process can beset by the vertical baffle to achieve.

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2011年12月21日星期三

Floating head heat exchanger

Floating head heat exchanger
Floating head heat exchanger tube plate at one end is fixed, rigid connection with the shell, the other end of the tube sheet is active, the end of the floating head heat exchanger tube plate is fixed, rigid connection with the shell, the other end of the tube plate is active between the shell and is not connected, as shown. Activities referred to as floating head tube sheet side, between the floating head is not connected to the concrete structure.

Floating head heat exchanger tubes can be withdrawn from the shell, so the tubewall for easy cleaning, tube bundle in shell in free expansion, so no thermal stress; but the complex structure, high cost, floating head office will result in two if Mifengbuyankinds of fluid mixed and difficult to detect. Floating head heat exchanger for a largertemperature difference between hot and cold fluids, dielectric constant need to be cleaned easily scaling the occasion. Used in various types of chemical production inshell and tube heat exchanger in the floating head up.

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Pressure vessel welded joints requires

Pressure vessel welded joints requires the choice of testing methods
1. Pressure vessel wall thickness of 38mm or less, its butt weld butt joints should be used in ray detection; due to structural and other reasons, does not use radiationdetection may make use of ultrasonic testing. 540MPa tensile strength greater than or equal to the standard material, and the shell thickness greater than 20mm of steelpressure vessels, each butt weld butt joints in addition to radiographic inspection, should increase the local ultrasonic flaw detection;
2. Pressure vessel wall thickness greater than 38mm. The butt weld butt joints, such as the selection ray detection, the weld should be part of each ultrasonic flaw detection; such as choice of ultrasonic testing, the weld should be part of each ray detection, which should include all T-joints ;
3. Requires testing of the corner joints, T-connector, not the ray or ultrasonic testing, should be surface inspection;
4. Non-ferrous metal pressure vessel butt weld butt joints should be used in radiationdetection.

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2011年12月20日星期二

Metal Pressure Vessel Requirements

Stainless steel and nonferrous metal pressure vessel requirements
1. Pressure vessels and pressure components of non-ferrous metal manufacturing,shall meet the requirements of this order, we must also meet the special technical requirements or the requirements of the design drawings;
2. Stainless steel and nonferrous metal pressure vessel must have a special requestor a dedicated manufacturing plant site, not with the black metal mixed with other products or production. To keep the workplace clean, dry, and strictly control dust.Forming and welding, should meet the needs of special tooling and equipment;
3. Stainless steel and nonferrous metal pressure vessel requirements must controlsurface mechanical damage and splashes;
4. Stainless steel and nonferrous metal pressure vessel requirements generallyshould be gas shielded arc welding.

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The development of heat exchangers

The development of heat exchangers
With the development of production technology, the scope of application of variousheat exchangers are constantly developing the application of various heat exchangers are constantly developing. Such as heat exchangers for high temperature and pressure of the scope of application are constantly developing the heat transfer process, it was mainly used simple structure of the flexible pipe or tube heat exchanger.

However, due to the heat exchanger fluid handling capacity is small, prices high, can not meet the needs of modern large-scale installations, so as the structural materialand manufacturing process development, shell and tube heat exchanger is togradually extend to the application of high temperature and pressure of the occasion,this heat exchanger in foreign countries, the maximum working pressure of 84MPa,temperature of 1000 ℃.

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2011年12月16日星期五

Stainless steel reactor main components

Stainless steel reactor main components of the device
Stainless steel reactor supporting a number of functional magnetic stirrerreactor, Weihai Chemical Machinery Co., Ltd. Universal stainless steel tube reactorto make up a number of irrational rotation around the light source and multi-tubemechanical rotation of the drawbacks of poor performance can be achieved at the same time, some inflatable tube function, multi-tube magnetic stirrer reactorperformance real practical value!

As the user due to the production process, operating conditions vary, the stainless steel reactor lid opening process, mixing pattern (with paddle, anchor type, frametype, spiral type, etc.), bearing type (type bearings suspended or supported ) andpacking devices, different requirements, contact the factory with a separate design.

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Steel pressure vessel weld heat treatment

Steel pressure vessel weld heat treatment
(1) pressure vessel steel weld heat treatment after the heat treatment should be usedas a whole. Like to take sub-heat treatment, heat treatment of their overlapping length should be not less than 1500mm. Outer part of the furnace insulation measuresshould be taken.

(2) steel pressure vessel weld heat treatment girth welds and repaired welds,allowing the use of local heat treatment. Local heat treatment of the weld, to includethe entire weld. Heat weld width on each side of not less than twice the thickness ofthe shell name; near the heated parts of the shell insulation measures should be taken.

(3) pressure vessel steel weld heat treatment should be ended and all the welding work experience received after passing the pressure test before.

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2011年12月15日星期四

Heat exchanger splicing

Heat exchanger splicing, should meet the following requirements:
a, butt joint welding process should be assessed. Number of specimen number, size, test methods according to the provisions of JB 4708; aluminum, copper, titanium welded joints or the reference implementation;
b, with a heat exchanger tube butt weld, not more than one straight; U-shaped tube not more than two; the shortest tube length not less than 300mm; including at least 50mm of straight pipe U-bend pipe welding splicing within the prohibited joints;
c, groove pipe end should be processed by mechanical methods, should be cleaned before welding;
d, corresponding amount of the wrong side of the wall thickness should not exceed 15% of tubes, and not greater than 0.5mm; straightness deviation will not affect the smooth tube wear limit;
e, the table should be selected after docking the diameter of the welding head to pass the ball checks to the ball by qualified;

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Pressure Vessel Weld Undercut

The surface pressure vessel weld undercut weld surface quality:
(1) pressure vessel weld surface quality of the weld surface undercut the standardtensile strength greater than 540MPa steel and Cr-Mo low alloy steel pressure vessel, made ​​of austenitic stainless steel pressure vessels, cryogenic pressure vessels , spherical pressure vessels and weld factor of 1.0, pressure vessel, the weldsurface may not have undercut;
(2) above (1) outside the pressure vessel weld surface of the undercut depth of notmore than 0.5mm, undercut shall not exceed a continuous length of 100mm, total length of weld undercut on both sides of the weld length shall not exceed 10%;
(3) non-ferrous metal pressure vessel weld undercut surface shall meet thestandards.

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2011年12月14日星期三

Pressure vessel for inspection holes

Pressure vessel for inspection holes (except heat) requirements
1. Pressure vessel shall have the inspection hole. Check the hole, includingmanholes, hand holes, threaded pipe plug inspection hole.
2. Than or equal to 1000mm diameter pressure vessel, shall be open at least onehole; pressure vessel inner diameter greater than or equal less than 500mm ~1000mm, should be open a hole or two hand holes; pressure vessel diameter lessthan or equal to 300mm ~ 500mm, should be set up at least two hand holes.
3. Circular manhole diameter shall be not less than 400mm, oval-shaped peopleshould not be less than the pore size 400 × 300mm; round hand hole diameter should be not less than 100mm, oval hand hole size should be not less than 75 × 50mm.
4. The pressure vessel has a removable head (cover and the like), or other cover toswitch, where people can play the role of hole or hand hole, can no longer set themanhole or hand hole. But its size, should not be less than the replaced provisionsmanhole or hand hole size.
5. Such as pressure vessels set on threaded pipe plug inspection hole (Note 3), you can not set the hand hole. Threaded pipe plug shall not be less than the nominaldiameter of 50mm.
6. Check the location of the hole opening should be reasonable, appropriate, easy to clean interior. Hand hole or threaded pipe plug inspection hole should be closedwere opened at both ends of the head or near the cylinder head on.
7. Spherical pressure vessel of the manhole should be located in the very belt.

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2011年12月9日星期五

Double glass reactor malfunction exclusion

Double glass reactor malfunction simple exclusion
1 Open the double glass reactor power switch, indicator light does not shine. External power supply or bad, please do not pass the professional electrician check thepower outlet.
2 fuse circuit, the double glass reactor power switch in the OFF position, and back toset fuses.
3 double glass reactor power indicator light, but does not rotate. Axis of rotation ruststop using, contact the vendor motor, electrical box is not connected seven-pin plugfailure to reconnect seven-pin plug
4 double-layer vacuum glass reactor suddenly disappeared, there are cracks in the glass, the switch checks the glass parts are damaged, transfer switch
5 double glass reactor with a vacuum, but not on the pumping ring wear, leaks, replace the connecting ring vacuum switch, switch

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Heat exchanger tube bundle problem

Heat exchanger tube bundle problem
The heat exchanger baffles, fixed rods, tube plates, and floating head cover, etc.,should be visually inspected to confirm the availability of corrosion and deformation,check the gasket for damage or aging. Check the heat exchanger tube plate and thehead without distortion.

The heat exchanger tube bundle thickness measurement is to check one of the basic content. The results of previous thickness measurements should be recorded forcomparison and trend analysis. An outer tube of the fin thickness depends on a dedicated ultrasonic thickness measurement probe or eddy current probe from thetube for testing. Sometimes, you can also use the sampling approach to treatment.

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2011年12月8日星期四

Guidebooks double glass reactor

Guidebooks double glass reactor
1, double glass reactor with a carefully before examination, and whether there isbroken glass, the interface is consistent, attention gently.
2, double glass reactor with a soft cloth (napkin available alternative) to clean theinterface, and then smear a little vacuum grease. (Vacuum grease after use must becovered to prevent dust sand to enter.)
3, the interface is not over-tighten, loosen regularly active, cause the connector to avoid long-term locked killed.
4, first open the power switch, and then let the double glass reactor from slow to fastrunning, shutdown the machine is stopped to make, and then switch off.
5, double glazing throughout PTFE reactor had to tighten the switch can not be easy to damage the glass.

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Fiber welding of plate-fin heat exchanger

Fiber welding of plate-fin heat exchanger
Welding of the fiber plate-fin heat exchanger, in addition to a collection box for both sides and weld thickness for surface crack detection, the main vacuum leak through the sides, respectively, to confirm their status. If the pressure test and found a leak,more easily found.

If leakage can be cut either side of the collection box, with another example of fillingpressure method, to identify the specific leak channel, for repairs to provide the correct basis. If the plate-fin heat exchanger is used for air separation plant in the main evaporator, in order to prevent the operation of liquid oxygen in the carbonmaterial should be kept within the plot is usually the oxygen leak channel blocked.Therefore, when conducting the leak. Channel should be inflated in nitrogen, oxygengas tank side of the cut set.

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2011年12月7日星期三

Operation of the external heat exchanger

Operation of the external heat exchanger inspection
A, heat exchanger base and bearing inspection. The basis of the heat exchangeris generally added by the saddle bearing concrete foundation formed, there are a fewof the heat exchanger are the basis of bearings and steel. On the concrete foundationshould first be visually inspected for cracks, spalling. The site of the suspectedsample can be checked. The heat exchanger shell and the gap between the saddle,should be carefully examined to confirm whether they occurred due to presence ofwater vapor corrosion. The saddle is usually welded with the heat exchanger shell. In this case, you should check the saddle between the anchor bolt hole and foundationbolts if there is room for expansion and contraction, and make sure not to tighten the bolt, one end of the saddle can move freely. Application Level check the concrete foundation subsidence, and visual inspection of the piping is related to the occurrence of distortion. If necessary, can be combined with vertical and horizontalhanging instrument measured way to verify the level of degree.

B, heat exchanger piping inspection. Running in the heat exchanger can beconnected to its external takeover checked for leaks. Operation were found to havesevere leakage nozzle, the suspension should be open connecting flange, replace the gasket, check the flange seals have groove-like damage.

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2011年12月5日星期一

Heat Exchanger Inspection Program

Heat exchanger inspection program should normally be processes and equipmentmaintenance management operations department in consultation with departmentsto determine. Plant operations department can process operating conditions,material changes in composition and other parameters to determine the overall heat transfer performance of heat changes and confirm the leakage situation.

Equipment maintenance management process operation according to the preliminary findings, combined with past history, the focus of this inspection to determine the content and focus area. Heat exchanger pressure shell, head, pressure vessels belonging to the scope of the inspection so they should first refer to the labordepartment in-service pressure vessel safety supervision requirements made ​​by the technical aspects of security checks.

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Reactor operation checks

Reactor operation checks

1 reactor before the operation to prepare the necessary driving tools such aswrenches, pipe wrenches, etc.;
2. checked before reactor operation safety valve, explosion-proof membrane,pressure gauges, thermometers and other safety devices are sensitive good
Use, safety valve, pressure gauge is in the calibration period, and the seals intact, the red line gauge whether the program is correct;
3 reactor operation checks reactor flange and base such as whether the bolts loose,security guard is intact and reliable;
4 reactor operation checks to confirm the device with a blue clamp Dafa no loosening, no small number, no residue, and arranged with a uniform distribution;
5 Confirm reactor operating oil level in sight glass reducer 1 / 2 to 2 / 3 between theautoclave box with a mechanical seal oil ring oil level higher than the static and dynamic sealing surface;

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2011年11月30日星期三

Pressure Vessels Process Parameters

Pressure vessels operating in the control of process parameters
1, the pressure vessel temperature control:
For the strict control of temperature, from the following measures: remove the heat of reaction; correct choice of heat transfer medium; enhanced insulation measures.
2, pressure vessels feeding control:
1), the exothermic reactor, feeding amount and speed can not exceed the capacity ofheat transfer equipment;
2), the ratio of reactants should be strictly controlled, to participate in the concentration of reactants, flow analysis and measurement to be accurate;
3), note that the order is expected to vote, can not be reversed;
4), raw materials, impurities can not be exceeded.
3, the amount of pressure vessels, filling the control:
General storage of liquefied gas containers installed capacity is 0.9 to 0.95 times the volume.
4, pressure vessel pressure, temperature fluctuation control
5, the control of corrosive media, pressure vessels.

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Tips to Run Reactors

To ensure uniform and rapid response can be carried out to improve efficiency, usually in the reactor is equipped with the appropriate mixing device, so they bringdynamic shaft seal and prevent leaks.

Reactor mostly clearance operations, sometimes in order to ensure product quality,after each batch of material are required to clean; kettle equipped with a quickopening manhole top and hand-hole, Shenzhen, network optimization, ease ofsampling, the measured volume to observe the reactions and to enter internalinspection devices.

Automated and continuous production of the gap instead of heavy manualoperations, such as the use of process control, can guarantee stable production,improve product quality, increase revenue, reduce manual labor, but also to eliminatepollution of the environment. Therefore, the resistance wire and the reactor body is not the space formed between the gap.

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2011年11月29日星期二

Selection Pressure Vessel Safety Valve

The selection pressure vessel safety valve should be consistent with the following eight principles:
1, the pressure vessel safety valve should be considered the choice of process conditions and container properties of the working medium, heavy volume leakagefrom the container security, physical and chemical media, working pressure range ofsecurity features and other considerations.
2, the safety valve must not be less than it is to send the heavy volume of safety ventheavy volume.
3, for the low working pressure, high temperature nor the pressure vessel can be used vibration lever safety valve.
4, from a closed structure, pressure vessels for high pressure, large containers anda large security leaks in heavy volume, the best choice of all the container from thelow-pressure safety valve, for the smooth operation of the absolute pressurecontainer safety valve should be selected from the micro.
5, for the costumes of toxic, flammable, or pollution of the environment of the mediashould be used in a closed pressure vessel safety valve.
6, the choice of reactor safety valve, the pressure must also consider the scope ofwork.

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Steam Autoclave Reactor Installation

Steam autoclave reactor installation:
1, steam autoclave  reactor should be installed on a sturdy, flat table, table height determinedbased on usage, equipment and table four weeks should be left a certain space (≥ 360cm), for the installation and later maintenance.
2, steam autoclave  reactor installation requirements to the horizontal shaft and vertical, notvertical (tilt) equipment shall not be greater than the total height of 1 / 1000.
3, the device itself from the process to take over the spare parts, safety valve, must be equipped according to the requirements of the reactor.
4, steam autoclave reactor installation check all parts and transmission parts are solid and reliable, the connecting pipe, nozzle, gas-tight seal and do the whole test, should be no bubble, run, drip, drain phenomenon.
5, the steam autoclave reactor into gear before starting the # 46 machine oil, open handrotating fan motor enclosure card lazy to check for the phenomenon, the phenomenon of impeller without scraping the wall, clean the dirt inside the reactor before startup.Empty running 30 minutes no unusual noise, vibration, before the official feed production. Periodic replacement of the other production slowdown as oil.

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Keywords: reactor, heat exchanger, pressure vessel

2011年11月28日星期一

Details Characters of Large-capacity Reactor

Large-capacity reactor has the following characteristics:

Throughput - high-capacity single-vessel wall reactor to replace the traditional jacketed vessel wall, the reaction vessel does not bear or bear only a small external pressure, and thus get rid of the traditional external pressure vessels as volume increases with to the vessel wall is too thick, heat transfer and other adverse factors, making the volume of reactor volume up to 30m 3, and even more, which greatly increased the production capacity of a single reactor.

High heat transfer coefficient - the heating and cooling the reaction medium are used built-in plate heat exchangers, heat transfer coefficient than the traditional coil heat exchanger is 40%, and the plate heat exchanger structure is more compact, more conducive to the volume The layout of the reactor large enough area of ​​heating and cooling, the resin synthesis process of a more uniform and stable.

Easy to maintain - as built-in plate heat exchanger is removable, so easy to clean and repair, helps to reduce operating failures, improve production stability.

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Keywords: reactor, heat exchanger, pressure vessel

2011年11月23日星期三

Pressure Vessels thermometer points

The safe use of pressure vessels thermometer points

1, should be the appropriate choice of measurement points, the temperature measurement point representative of the situation and minimize the impact of external factors. The installation location should be easy to observe operating personnel, and equipped with explosion-proof lighting.

2, the thermometer should be inserted into the package temperature or pressure vessel close to the pressure vessel wall, while exposed parts should be as short as possible to ensure accurate measuring container medium temperature.

3, for the medium temperature pressure vessel conditions of rapid change, when thetemperature lag effect should be taken into account.

4, pressure vessels thermometer installed in the easy, free from collision to reduceshock location.

5, the newly installed national metrology department thermometer should beaccredited.

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Temperature Problem of Heat Exchanger

Heat exchanger in the relative flow of fluid downstream and upstream are generally two. Downstream, the maximum temperature difference between the two fluids at the entrance and along the heat transfer surface, gradually reducing to a minimum temperature at the exit. Reflux, the two fluids along the heat transfer surface temperature distribution is uniform. In the cold and hot fluid inlet and outlet temperature under certain conditions, when the two fluids are no phase change, the maximum temperature difference in the average upstream downstream minimum.

Upon completion of the same heat transfer (Heat exchanger)conditions, using counter-current can increase the average temperature difference, heat exchanger heat transfer area is reduced; if the heat transfer area of ​​the same, using reflux heating or cooling fluid can reduce consumption. The former can save equipment costs, which can save operating costs, it is used in the design or production should maximize the use of the countercurrent heat exchanger.


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Keywords: reactor, heat exchanger, pressure vessel

2011年11月22日星期二

Electric heating - reactor

Electric heating - reactor

The resistance wire wrapped around the reactor tube insulation, or installed in the reactor a certain distance away from the ad hoc insulator, and therefore the resistance wire in the reactor body with a small space between the gap.

The first three methods are required to obtain high-temperature reactor body in addition jacket, due to temperature change, causing the jacket and the reactor shell to withstand temperature changes resulting from temperature stress.

The use of electric heating equipment lighter is simple, easier to adjust the temperature, and do not pump, stove, chimney and other facilities, starting is very simple, not high risk, low cost, but operating costs than other heating methods, thermal efficiency below 85%, it is applied to the heating temperature below 400 ℃ and at places of lower energy prices.

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Pressure vessel pressure gauge

Pressure vessels and pressure equipment need to control the pressure gauge must be installed. Install pressure gauge is to measure the pressure medium pressure vessel, the operator can be indicated by the pressure gauge to operate, the pressure control in the permitted range.

Classification and working principle of gauge
Pressure gauge (pressure vessel) is divided into four categories: liquid column type,elastic components, piston and power type.
Elastic element type is now widely used, mainly because the pressure gauge withsolid structure, not leak, high accuracy, easy installation, wide measurement range,low price, etc..

Pressure vessel pressure gauge works: medium pressure acting on the fixed end ofthe spring tube, so that the free end of the spring tube driven by the pull rod bent lever,turn the pointer to show the pressure.

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2011年11月21日星期一

Multi-layered Pressure Vessels

According to structure, can be divided into multi-layered pressure vessels, pressure vessels around the plate, with a groove around the pressure vessel, heat set pressure vessels, pressure vessels and forge-welded plate roll-welded pressure vessels. Most of the pressure vessel made ​​of steel and some aluminum, titanium and other non-ferrous metals and glass, steel, prestressed concrete and other non-metallic materials.

Pressure vessels in use in the event of an explosion will cause a catastrophic accident. Pressure vessel in order to ensure the safety of the premise to advanced design, reasonable structure, easy to manufacture, use, reliable and cost of economic purposes, countries are in accordance with its specific conditions on the pressure vessel standards, specifications and technical conditions of pressure vessels the design, manufacture, testing and use of concrete and must comply with the regulations.


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Partitions and Tube Heat Exchanger

Partitions heat exchanger

Heat exchanger is the chemical, petroleum, power, food and other commonequipment in many industrial sectors, plays an important role in the production in thechemical production in the heat exchanger can be used as heater, cooler, condenser, evaporator and reboiler etc., used more widely. Many different types of heat exchangers, but according to cold and hot fluid heat exchange principles and methods are basically divided into three categories namely: partitions type, hybridand regenerative. In the three types of heat exchangers, heat exchanger partitions the most widely used.


Tube heat exchanger

Tube (also known as shell and tube, and tube) heat exchanger is the most typicalpartitions heat exchanger, industrial applications it has a long history, and all of the heat exchanger is still dominant. Tube heat exchangers are shell, tubes, tube sheetand seal top part, the shell mostly circular, parallel with the internal control, fixed at both ends of the tube bundle panel.

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2011年11月18日星期五

Variety of pressure vessels division

 Variety of pressure vessels division

Pressure vessels in the production process by the action principle, divided intoreaction pressure vessels, pressure vessels, heat exchangers, pressure vessels,separation, storage pressure vessel. Specific divided as follows:

(1) reaction pressure vessel: the medium is mainly used to complete the physical,chemical pressure vessels, such as reactor, reaction kettle, decomposition of the pot,autoclave, decomposition tower, polymerization autoclave, autoclave, high pressurereactor, reactor , shift converter, cooking pot, steam ball, autoclave, gas heaters.

(2) heat exchanger pressure vessel: is mainly used to complete the heat exchangemedium pressure vessels, such as shell and tube heat boilers, heat exchangers, coolers, condensers, heater, sterilizer, dyeing device, dryer, steaming wok, warm the pot, solvent preheater, steamer, steam offline, electric steam generator, gas furnacewater jacket and so on.

(3) separation of pressure vessel: the medium is mainly used to complete the bufferfluid pressure balance between separation and gas purification pressure vessels,such as separators, filters, oil, buffers, scrubbers, absorption tower, copper scrubber,drying tower, stripper, sub-cylinder, oxygen, etc..

(4) storage pressure vessel: mainly used for storage, dress gases, liquids, liquefied gases and other media, pressure vessels, such as various types of tanks.

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The main features of double-reactor

The main features of double-reactor:

1 Frequency Control, AC induction motor. Constant speed, no brushes, no sparks,security and stability, continuous work.
(2) full glass apparatus (reactor) using borosilicate glass GG17, good chemical and physical properties.
3 glass interlayer interfaces pass through the loop on the hot oil, do the heatingreaction liquid can be frozen through the low-temperature reaction.
4 reaction at room temperature, through the water that will reflect heat away quickly.
5 port decentralization spout with flange and PTFE valve, the container is no dead ends, removable to facilitate the discharge of solid materials.
6 four reactor cover (reactor), large mouth design for easy cleaning, standardinterface socket assembly back option, distillation synthesis device.

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2011年11月17日星期四

Gas scrubbers (heat exchanger)

 Gas scrubbers (heat exchanger)

Petrochemical production process (heat exchanger)often encountered dust and gas, using a largecyclone dust particles can only get rid of. Is to pass into the dusty gas scrubber. Full access to gas and water droplets, the adhesion of solid particles by water, with thebottom of the outflow, the gas which has been purified. High collection efficiencyusing this method, but the water consumption, gas humidity increases, the temperature decreased, large sewage treatment. Only in plenty of water, sewage treatment conditions can conveniently use.

Hybrid condenser (heat exchanger) has a simple structure, high efficiency heat transfer, corrosion problems are relatively easy to solve.

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Stainless Steel Reactor in Driving

Stainless Steel Reactor in Driving

1, the feeding should be preceded open agitator reactor, no noise, and normal, thematerial added to the reactor, the feed must not exceed the number of process requirements.
2, open the steam valve before opening the valve back, entered after the valve. Open the steam valve should be slow, so warm up on the jacket, the gradual step-up, the jacket pressure must not exceed the specified value.
3, the steam valve and cooling valve can not start, no-steam pipe passing hammerand collision gas.
4, open cooling water valves, the first open return valve, the latter entered the valve.Cooling water pressure not less than 0.1 MPa, was not allowed higher than 0.2 MPa.
5, the water ring vacuum pump, the pump after the first open water, stop the pumpwhen the pump stops after the first water, and water pump should be excluded.
6, always check the reactor operation, and found that exceptions should be shut down for maintenance.
7, cleaning titanium epoxy (enamel) reactor, the reactor are not allowed to use alkaline brush, be careful not to damage the enamel

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2011年11月16日星期三

Reactor temperature problem

Reactor temperature problem
(Reactor) reaction temperature and time when the reaction mixture temperature is below 80 ℃, if the ammonium chloride as a catalyst, the ammonium chloride reaction speed, PH value not show up until after the temperature, PH value decreased rapidly , the reaction speed, resulting in gel polycondensation reaction is too intense and appear sticky wall.

In addition, the (reactor) polycondensation reaction time is too long, resin molecular weight, viscosity is too high the wall is also prone to sticky phenomenon. Therefore, the operator should be properly controlled polycondensation reaction temperature and time, time to stop the reaction. General reaction solution temperature was controlled at ~ 95 ℃ or less appropriate.


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Non-metallic Materials Heat Exchanger

Non-metallic materials heat exchanger according to principles of classification:

Direct contact heat exchanger
This type of heat exchanger and the operating principle is to contact each other by two media heat transfer, heat transfer achieved, the contact area directly affect the heat transfer, heat exchanger of this type of media is usually one is gas and another for the liquid The main tower is a heat transfer device as the main equipment, but usually also involves the mass transfer, it is difficult to distinguish between the relationship with the tower, usually under the jurisdiction of the tower equipment, power plant cooling tower is the most typical for direct-contact heat.

Storage heat exchanger (the accumulator), very little amount of such heat exchangers, the principle is to heat the heating medium to pass solids up to a certain temperature, the cooling medium through the solid material is heated, so heat transfer to reach purposes.

Partitions heat exchanger
Such very large amount of heat, more than 99% of the total, the principle is the medium through metal or hot heat transfer to the cold medium, such as heat exchanger shell and tube we usually, plate, plate-fin type or shell type heat exchanger.

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2011年11月15日星期二

Hybrid heat exchanger gas scrubber

Hybrid heat exchanger gas scrubber (or scrubbers)

In the industrial use of hybrid gas scrubber heat exchanger equipment to wash the gas that has a variety of purposes, such as gas mixture with the liquid to absorbsome of the components, in addition to net gas in the dust, gas humidification ordrying, etc. . However, its most widespread use of the cooling gas, and cooling of theliquid, mostly water. Widely used in air conditioning engineering spray chamber, itcan be considered a special form.


Not only can spray chamber as gas scrubbers (hybrid heat exchanger) for cooling the air, like, but also its heat treatment. However, it also has high requirements for water quality, large area, water pumps and other energy-consuming and moreDisadvantages: So, now in general construction, the spray chamber has been rarelyused or used only as a humidification device. However, in order to adjust the humidityas the main purpose of the textile mills, cigarette factories, are still a lot of use!

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The use of glass-lined reactor Notes

The use of glass-lined reactor Notes:


Extensive use of glass-lined chemical industry reactor, due to the corrosive medium, the reaction conditions, hot and cold, transport, use, human and other issues, therewill always reactor such as the enamel layer is damaged, resulting in unnecessaryproduction stops, such as off a large area, it is recommended only returned to the manufacturer to re-enamel.


Enamel kettle reactor higher prices, little damage is not necessary to update the entire device, which requires the appropriate choice of repair method was used(fresh element into) JS916 repair immediately, otherwise, it will make the reactor vessel where the solvent is corrosive , the damage to the enamel surface will rapidlyexpand, and the resulting cut-off, accidents and environmental pollution can not be anticipated losses.

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2011年11月14日星期一

Introduction to plate heat exchanger

 Introduction to plate heat exchanger

Plate heat exchanger by a high-definition map of the plate heat exchanger equipment, balance tank, centrifugal sanitary pumps, hot water unit (including steampipes, hot water sprayed into the device), stands and instrument boxes and other components. For milk or other heat-sensitive liquid sterilization cooling. To deal withthe material balance of the first into the slot, by sanitary centrifugal pump into the heat exchanger, after preheating, sterilization, heat, cooling sections, have not metsterilization temperature of the material, the instrument control for the air return valve, and then back to balance tank re-processing.


Plate heat exchanger material sterilization temperature automatically by theinstrument control box controls and continuous recording, in order to monitor thesterilization process and inspection. This device is suitable for pre-sterilization ofmilk, Pakistan sterilization. Plate heat exchanger plate heat exchanger type mainframe (removable) and brazed into two categories, the main form of chevron platecorrugated board, corrugated board and the level of flat-shaped plate three kinds oftumor.

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Advantages of ceramic heat exchanger

Advantages of ceramic heat exchanger
Ceramic heat exchangers used in metal heat exchanger limitations have been well under development, as it has solved the corrosion resistance, high temperature and other issues, recycling has become the best high-temperature heat exchanger. After years of production practice, indicating that the ceramic heat exchanger with good results.

The main advantage of ceramic heat exchangers are: thermal conductivity, high temperature strength, oxidation resistance, thermal shock resistance. Long life, small amount of maintenance, reliable performance, easy to operate. High-temperature flue gas heat recovery is the best device.


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2011年11月11日星期五

Features electric heating reactor

 Features electric heating reactor

Electric heating reactor with rapid heating, high temperature, corrosion resistance, hygiene, no pollution, no automatic heating boilers, easy to use and so on. With electric heating rods inside the jacket heat-conducting oil, the heat transfer oiltemperature rose to the desired temperature, then heating with temperature controldevice controls power to help make the period of constant temperature.

Electric heating reactor in absorbing foreign advanced technology, based on thesuccessful development of new products, widely used in pharmaceutical, chemical, food, natural seasonings, food additives, light industry and other industries.

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Pressure Vessel - Waste heat boiler

Pressure Vessel - Waste heat boiler
Waste heat boiler (third class pressure vessel) from the drum, event hoods, mouth section of the flue, flue paragraph 1 oblique, oblique section of the flue 2, the end of a section of the flue, the flue end of paragraph 2, the feeding tube (cutting slip) tank, oxygen muzzle, nitrogen and nitrogen seal plug seal device, manholes, micro-differential pressure measuring device, the flue and hanger bearings and other components.

Waste heat boiler (third class pressure vessel) is divided into six cycle loop, each loop route back down the riser pipe and components, each section of the flue pipe water down from the drum through the introduction to each flue after the next set of boxes into the heating surface, water vapor through the heating surface resulting from the import into the collection box, and then by the introduction of the drum riser. Between the various flue are flanged.


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2011年11月9日星期三

Plate heat exchanger

Plate heat exchanger
It is a new and efficient heat exchanger, composed of many thin parallel plates made ​​of metal.

Each plate heat exchanger, said metal plates are uneven stamping rules ripplesaround between adjacent panels with two gaskets, combination plates are pressedclose around together with the gasket, sealing between the plate the gap. Differentthickness of the gasket can adjust the distance between two board to change thechannel cross-section size.

Plate heat exchanger on the four corners of each plate to open a channel each, two of which channel the board with a gasket and separated flow, and the other two flowchannels connected with the board, both in the adjacent fluid through the pore the twoboards are staggered, hot and cold fluid at the same flow on both sides of the plates, in addition to both ends of the board, each board is a plate heat transfer surface.

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Autoclave reactor fluxes measuring

Autoclave reactor fluxes measuring device applications

Autoclave reactor fluxes measuring device placed in the reaction vessel containing the γsources, the upper and lower detectors, detector followed by a signal processing part and then change the control part, and ultimately by the output of a proportional, theproduct of the current under the detector counting signals to characterize the amount of reactor materials, the device address in the supercritical operating conditions can not be on-line monitoring the amount of reactor materials and continuous production.


Reactor - Backflow device including pressure pump shear, compression and shear mixingpump pumps, extrusion pumps include mixing tube, outer tube, spindle and mixingboard, the formation of the outer tube and inner tube jacketed hollow spindle through the bracket pipe connections, including fixed, fixed with oblique spindle mixing board;shear pump, including shelters, attendance sheet, under the cover and Xiazuo board,there are cloth panels with attendance expected to cover the hole fixed connection,Xiazuo board with the material on the next hole and cover with the connection pinfixed in the next seat panel to set the material in the attendance sheet hole; pressurepump inlet pipe through the back connected with the bottom of the reactor, the pressure pump outlet and squeeze the bottom of the mixing pump connected to the upper extrusion and shear mixing pump cover pump inlet connection, cut the pumpdischarge port is located under the cover on top of the reactor.

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Pressure vessel Application examples

Pressure vessel Application examples - reactor

Reactor (pressure vessel) is widely used in petroleum, chemical, rubber, pesticides, dyes, pharmaceuticals, food, used to complete the curing, nitration, hydrogenation,alkylation, polymerization and condensation process of pressure vessels, such asreactor, reaction pot, pan decomposition, polymerization reactor, etc.; materialsgenerally have carbon-manganese steel, stainless steel, zirconium, nickel (Hastelloy,Monel, due to health nickel) alloys and other composite materials.


According reactor (pressure vessel) manufacturing flat structure can be divided intoopen-type reactor lid, welded flange open and closed reaction vessel reactor three categories.

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2011年11月8日星期二

Plate heat exchanger vs tube heat exchanger

Plate heat exchanger vs tube heat exchanger

Plate heat exchanger tube heat exchanger with the difference between what?
Plate heat exchangers are highly efficient heat transfer equipment. In practice, there are two, one is the umbrella spinning method of manufacturing plate heat exchanger, the other is the stamping method of manufacturing flat-panel heat exchanger, its structural features are as follows: Plate heat exchanger small, small footprint. Plate heat exchanger area for the same heat transfer capacity of heat exchanger tube about 30%, if sprinkled with cream-style row tube cooler compared to the superior.

Plate heat exchanger heat transfer efficiency. Plate heat exchanger to make two kinds of heat exchange fluid at a low flow rate, the enhanced disturbance, provoked turbulence, which enhanced heat transfer, heat transfer coefficient K up 16720J / (m2 • h • ℃) (water to water ), higher than the heat exchanger tube 2 to 4 times. Plate heat exchanger assembly flexible. When the production process conditions and production requirements change, the plate heat exchanger plates as long as the increase or decrease the quantity or change the channel plate assembly process the form, you can meet the requirements. Plate heat exchanger metal consumption is low. Plate heat exchanger made of stainless steel or titanium to suppress the main heat transfer, sealing pads, clamping bolts and pressure plate frames and other parts of the whole composition. Plate heat exchanger plate is 8kg metal consumption per square meter, while the same parameters of the spiral plate heat exchanger requires about 20kg, shell and tube heat exchangers of other even more.

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Keywords: Reactor, heat exchanger, pressure vessel

2011年11月4日星期五

Conditions of pressure vessel technology

Conditions of pressure vessel technology

1) conditions are harsh. Pressure vessels of different sizes will not only bear the pressure of the load (in general, or pulsating load) and other loads, and some still in high temperature or cryogenic operating conditions, the working medium is oftencorrosive, relatively harsh environmental conditions .

2) pressure vessel - easy to overload. Pressure inside the container is often due to operational errorsor abnormal reaction increased rapidly, and often not found in the case of rupture ofthe container already.

3) pressure vessel - the local stress is more complex. For example, around openings in the containerand other structural discontinuities, often due to high local stress and repeatedloading and unloading caused by fatigue cracking.

4) pressure vessel - often hide serious defects. Welding or forging containers, often left behind in the manufacture of small cracks and other serious defects, which, if expanded in the operation of, or in appropriate conditions (such as temperature, nature of the working medium, etc.) will cause a sudden rupture of the container.

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Pipe Heat Exchanger

Pipe heat exchanger is controlled by the diameter of the different straight into theconcentric tube, connected together by the U-shaped bend in the heat exchanger, a fluid within the tube, and another annular fluid away , both can get a higher flow rate, so the heat transfer coefficient. in addition, the tube heat exchanger, two fluids forpure counter-current, large logarithmic mean driving force.

Simple tube heat exchanger, can withstand high pressure, the application is also convenient (subject to increase or decrease the number of pipe), especially sinceboth tube heat exchanger with heat transfer coefficient, heat transfer driving force can be big and strong to withstand high pressure the advantages of the high pressureproduction process (such as operating pressure of 3000 atmospheres pressurepolyethylene production process) in the heat exchanger used in almost all tube type.

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2011年11月1日星期二

Rotary wheel heat exchanger

Rotary wheel heat exchanger to the whole 10/20 rev / min rotation speed constantly, constantly turning the wheel as a heat storage / storage-core body, fresh air through the heat exchanger of the semi-circular wheel, while the exhaust reverse through the wheel of another semicircle. Fresh air and exhaust air in this manner by alternating reverse wheel, while the exhaust heat released into the heat storage / storage core body.

Rotary wheel heat exchanger: Type in the full heat wheel, the other is to ensure that transfer moisture. Separated from the water flow into the regenerator core body moisture coating, when the wheel to another when the air is released into the water.

Exhaust air heat exchanger is the use of whole and fresh air into the sensible heat and latent heat exchange and energy recovery, and thus to save energy and maintain good ventilation equipment. In the summer you can pre-cooling and dehumidification of fresh air, fresh air in the winter can warm humidification, the recovery efficiency of 75% or more, thus reducing the cooling load in air conditioning and power consumption.

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Keywords: Reactor, heat exchanger, pressure vessel

2011年10月30日星期日

Plate heat exchanger technology developments

Plate heat exchanger technology developments:

Anti-corrosion technology. This year, countries in the field of heat exchanger corrosion research and design has also made a more significant results, such as anodic protection technology development and application of new materials, corrosion is a type of heat exchanger so as to bring the development of the infinite of life. In addition, the application of non-metallic materials, heat transfer is greatly enhanced corrosion resistance.

Both large and miniaturization. With the large-scale sets of devices, heat exchangers the direction of the large-scale development, and in microelectronics, aerospace, medical, chemical and biological engineering, materials science and other occasions of special requirements to the miniaturization.

To strengthen the technology. Variety of new, highly efficient heat exchanger gradually replace the existing conventional products. Plant dynamic effect of enhanced heat transfer technology, additive enhancement of boiling heat transfer technology, through the enhancement of heat transfer into the inert gas technology, dropwise condensation technique, micro-heat transfer technology, the magnetic field power heat transfer technology, nano technology, heat transfer fluid will be research and development.


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Developments of Heat Exchanger

The structural characteristics of the evaporator plate and the use of

Either way the above changes, better use of the evaporator plate to play in that form of change, to find changes in the development of state development.

     Shell and tube heat exchanger is usually a fixed tubesheet, U-shaped tube and floating head three forms. Three structures have advantages and disadvantages for different occasions. Shell and tube heat exchanger as long as the shell, tube sheet, tubes, sealed top component composition.

     Although the shell and tube heat exchanger is a generalized product, but in conditions of varying heat transfer conditions, due to the limitations of its structure, hot and cold logistics operating conditions and physical properties of multilateralism, and the specific work conditions to optimize the design of the lack of means, often made of shell and tube heat exchanger heat transfer efficiency at a lower run, with the petrochemical and energy industry, the rapid development of enterprise energy research deepens, the recent development of many new processing technology, for example, heat exchanger networks using pinch technology, logistics and pre-heating process to increase recycling, reduce the heating or cooling load and utility consumption, has received very good results. However, the subsequent use of the system when the heat becomes more vast and complex, due to the depth of the heat recovery heat transfer temperature difference resulted in a significant decline in the heat transfer network, resulting in a sharp increase in heat transfer area, in order to improve heat transfer efficiency of heat exchangers, research is imperative to enhance heat transfer technology, the current involves the most extensive study was undoubtedly the deepest convection heat transfer technology. Previously, shell and tube heat exchangers used for baths bath, industrial demands for water continue to the industry, as well as features of the industry.

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2011年10月28日星期五

Reactor failure phenomena and solutions

 Autoclave Reactor failure phenomena and solutions:

A failure phenomenon: there is a leak at the valve.
Failure: Reactor stem (pin), valve port sealing surface damage.
Remedy: repair, replacement stem (pin), the valve port.
Symptom 2: outside the magnet rotates within the magnet does not turn the motorcurrent is reduced.
Cause: The temperature rise inside the reactor vessel is too high, resulting in poorcooling cycle, temperatures inside the magnet due to magnetic faded.
Hydrogenation reaction, there are cracks within the magnet sets, expansion within the magnet.
Remedy: notify supplier to replace the internal magnet.
Symptom 3: magnetic coupling within the actuator friction noise.
Failure: bushings, bearings wear, the gap is too large, there beats within the magnetrotation.
Remedy: Contact with suppliers, replacement bearings, bushings.
4, fault phenomenon: leakage at the sealing surface.
Failure: Reactor screw thread loosening; sealing surface damage.

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Laboratory reactor control theory

Laboratory reactor control theory

Control the reactor temperature to avoid internal and external temperature exceeds the maximum allowed. Heating reactor and when the cover must be careful,because they will lead to local temperature exceeds 350 ℃. When using a transformer, and gradually increase the voltage in the preparation period we recommend using 3 / 4 of the voltage (ie, half-power) until the internal temperature reaches your desired range, so as not to exceed the maximum temperature difference △ T. In the reactor in response to different media to do, you should firstfind out whether the corrosion medium on the subject material.

Of severe transient response, resulting in a large number of flammable gases orhigh-temperature chemical reactions, and high pressure, ultra-high temperature ormedium chlorine ions, fluoride ions on the corrosion of stainless steel have a severe reaction to be special orders. Set in the reactor with platinum resistance or thermocouple, using a different temperature difference into electricitytelecommunications number, transmission instructions to the temperature regulator,heating circuit using solid state voltage regulator to regulator, adjust thepotentiometer to change the size of the heating the size of the output voltage tostepless voltage regulation, if an appropriate adjustment can meet the purpose ofheating rate and temperature.

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2011年10月27日星期四

Glass and stainless steel autoclave reactor

Glass and stainless steel autoclave reactor used, what is the difference in

Advantages and disadvantages of both in stark contrast to the glass reactor has a very good chemical stability, excellent corrosion resistance, acid and alkali drawback is poor thermal conductivity of stainless steel reactor with excellent thermalconductivity drawback is the poor resistance to acid and alkali course this is the general direction of the above comparison is for the stainless steel reactor called the316L has a good material to make up for the shortcomings of acid and alkaliintolerance is very expensive, but you can both advantages and disadvantages of the choice of optimal.

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2011年10月25日星期二

Types of Hybrid Heat Exchanger

Hybrid heat exchanger is to rely on cold and hot heat transfer fluid for direct contact, this way to avoid heat transfer and heat transfer partitions on both sides of the fouling resistance, as long as the contact between the fluid in good condition, there is a large the heat transfer rate. Therefore, any occasion to allow the fluid mixed with each other, can be mixed heat exchanger, such as gas washing and cooling, cooling circulating water, steam - water mixture between the heating steam condensate, and so on. It can be applied throughout the chemical and metallurgical enterprises, power engineering, air-conditioning engineering, and many other manufacturing sectors.

According to different purposes, hybrid heat exchanger can be divided into several different types:

(1) heat exchanger cooling tower (or cooling tower) in this device, with natural ventilation or mechanical ventilation method, the production has increased the temperature of cooling water for cooling after the cycle in order to increase the economic efficiency of the system. Such as thermal power plants or nuclear power plants circulating water, ammonia production in the cooling water, cooling water cooling tower through recycling after use, this method in practical engineering has been widely used.

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Tube Heat Exchanger and Plate Heat Exchanger


Tube heat exchanger tube heat exchanger is controlled by the diameter of the different straight into the concentric casing, connected together by the U-shapedbend in the heat exchanger, a fluid inside the tube, and the other take a fluid annulus, which can be obtained with higher flow rates, so the heat transfer coefficient. in addition, the tube heat exchanger, two fluids for pure counter-current, largelogarithmic mean driving force. Simple tube heat exchanger, can withstand high pressure, the application is also convenient (subject to increase or decrease the number of pipe), especially since both tube heat exchanger with heat transfer coefficient, heat transfer driving force can be big and strong to withstand high pressure the advantages of the high pressure production process (such as operating pressure of 3000 atmospheres pressure polyethylene production process) in the heat exchanger used in almost all tube type.
Plate heat exchanger: the most typical partitions heat exchanger, industrial applications it has a long history, and all the heat exchanger is still dominant. The main structure of the heat exchanger plates and plates of the strip between the composition. Long-term dominance in the market, but its bulky, heat transfer efficiency is low, replace the expensive tape (tape replacement costs account for about 1/3-1/2 of the whole process), mainly used in liquid - liquid between the heat exchanger, often referred to as water of heat transfer within the industry, the heat transfer efficiency 5000w/m2.K.
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2011年10月23日星期日

Introduction of Energy-volume Heat Exchanger

Introduction of Energy-volume Heat Exchanger

Automatic temperature control, energy-volume heat exchanger, which make full use ofsteam energy, efficiency, energy saving is a new water heater. Ordinary water of heat exchanger heat exchanger configuration is generally required to reduce thetemperature of the steam condensate for reuse. The energy-saving condensing heat exchanger water temperature at 75 ℃ or so, back to the boiler room can be directlyreused. This reduces equipment investment, saving heat exchanger room area,thereby reducing infrastructure costs: so energy-efficient volumetric heat exchangerunit welcomed by the majority of design users.

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Reactor fermentation industry applications

 Fermentation industry is inseparable from stainless steel autoclave, in our lives a lot of items are generated by fermentation. Reactor  through the stainless steel fermentation industry has been driven more than a billion for the domestic and the international market with a lot of necessities of life food, such as spices, sour agent, highly active dry yeast, starch and starch sugars, organic acids, feed additives. In addition to the use of stainless steel reactor outside the above description of several new items have appeared, over the past decade to develop into industrial production of fermentation products with special features, such as oligosaccharide, fungal polysaccharides, sugar alcohols, active peptide, microbial agents, and biological preservatives, etc., to meet the health needs of different groups of people. Production of such goods before the time is very old, very old methods, now have such a good stainless steel reactor equipment to facilitate a lot, now manufactured by fermentation using microorganisms. I believe in the future fermentation industry, the better the performance.

This article provided by the Weihai Huanyu reactor: Reactor fermentation industry applications

Expand Keywords: heat exchanger, pressure vessel

2011年10月20日星期四

Volume and plate heat exchanger

Volume heat exchanger and plate heat exchanger

Volume heat exchanger and plate heat exchanger is the difference between the former has the ability to store large amounts of water, hot buffering capacity. Volume heat exchanger water capacity greater storage capability. But the appearance of larger, relatively low heat transfer efficiency. Compact plate heat exchanger, heat transfer coefficient is high, hot start quickly.

Heat exchanger is the tank volume, heat resistance, but more bulky covers, heat transfer efficiency is relatively low, scaling is not good cleaning. Install the high cost oftransportation problems. Compact plate heat exchanger, heat transfer coefficient is high, hot start quickly. However, the larger the internal resistance.

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Radiators and heat exchangers

Radiators and heat exchangers

Air-conditioning refrigeration cycle system in general by the compressor, condenser,throttle valve, evaporator and other components, which collectively referred to as the evaporator and condenser heat exchanger, copper and aluminum are two kinds ofmaterial
Material made ​​of. Generally U-shaped copper tube bent, U-shaped nozzle and then with the semi-circular welded pipe, made ​​of copper through the aluminum fin. Brasstube technology with expansion up to make close contact with brass and aluminum,two closely with each other vertically.

Radiator: Radiator is used to transfer, release heat range of devices collectively.There are currently radiator heating radiator, radiator computer.
Home heating radiators, central heating heat source for the city generally, communityself-built boiler room, home boiler, etc., by heat conduction, radiation, heat convectionto heat up, so that the room temperature may be raised. Currently on the marketheating radiator material is basically divided into the brass from aluminum finconvection radiator, steel radiator, aluminum radiator, copper radiator, stainless steelradiator, copper-aluminum composite radiator, etc., also with the original cast ironradiators.

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Variety of pressure vessels division

 Variety of pressure vessels division

Pressure vessels in the production process by the action principle, divided intoreaction pressure vessels, pressure vessels, heat exchangers, pressure vessels,separation, storage pressure vessel.

Specific divided of as  Variety of pressure vessels follows:
(1) reaction pressure vessel (code R): is mainly used to complete the physical media,pressure vessels, chemical reactions, such as various reactors, reactor,polymerization reactor, reactor, transform furnace, gas furnace and so on.
(2) heat exchanger pressure vessel (code E): is mainly used to complete the heatexchange medium pressure vessels, such as various heat exchangers, coolers,condensers, evaporators, and so on.
(3) separation of the pressure vessel (Code S): the medium is mainly used to complete the buffer fluid pressure balance and separation of gas purificationpressure vessels, such as the various separators, filters, oil, scrubbers, absorption tower, copper washing tower, drying tower, stripper, sub-cylinder, oxygen, etc..
(4) storage pressure vessel (code C, where spherical code B): mainly used forstorage, dress gases, liquids, liquefied gases and other media, pressure vessels,such as the various types of tank, buffer tank, sterilizer, dyeing machine, dryer,steamer, etc.
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2011年10月19日星期三

Glass and stainless steel reactor

Glass and stainless steel autoclave reactor

Advantages and disadvantages of both in stark contrast to the glass reactor has a very good chemical stability, excellent corrosion resistance, acid and alkali drawback is poor thermal conductivity of stainless steel reactor with excellent thermalconductivity drawback is the poor resistance to acid and alkali course this is the general direction of the above comparison is for the stainless steel reactor called the316L has a good material to make up for the shortcomings of acid and alkaliintolerance is very expensive, but you can both advantages and disadvantages of the choice of optimal.

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Keywords: reactor,pressure vessel,heat exchanger

2011年10月18日星期二

Titanium and stainless steel reactor

Features of Titanium and stainless steel reactor

Titanium reactor for laboratory dispersion, mixing, emulsification, homogenization,dissolution. Titanium reactor in vacuum or pressure conditions, the glass reactorthrough the material for the observation of the mixing, homogenizing, emulsifying, dispersing, mixing and other reaction. Titanium reactor can simultaneously measurethe material temperature, pressure, viscosity, PH and so on. Materials can also be heated or cooled.

Stainless steel reactor Scope: Suitable for petroleum, chemical, pharmaceutical,metallurgy, scientific research, universities and other departments for high-temperature, high pressure chemical reaction experiments, the viscous and particulate material can achieve high mixing effect.

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Classification of Electric heating reactor

Electric heating reactor enamel basic classification

First, the enamel of the electric heating reactor mainly by its pot, kettle lid body, the body kettle agitator, jacketed reactor body, reactor vessel body and the body supportgear, vessel and other components of the body seal device, it materials and openingthe process according to the requirements of our customers and develop.

Second, by the enamel forms of electric heating reactor heating reactor can be divided into electric heating, oil heating enamel reactor, steam heated enamelreactor, the reactor water heating enamel, fire and other heat-type reactor.

Third, according to its jacket into the form: jacketed reaction vessel and the outerenamel plate semi-tube type reactor, heat transfer oil or heating jacket are equipped with the type of diversion devices.

Fourth, enamel reactor in the form of electric heating in general there are paddle-styleanchor, frame style, thread style, scraping the wall box-style and so on. In contrast to these, high-speed reactor type is scattered on the main type of impeller, turbine, highshear, the propeller-type, according to its process for customers to choose.

Fifth, enamel electric heating reactor agitator drive is a common form of the mainmotor, explosion-proof motor, electromagnetic governor motor and the inverter, etc.,it has cycloid gear wheel, the worm style, infinitely variable speed planetary type and so on.

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Tips to Clean Reactor

Tips to Clean Reactor
A mechanical cleaning: high pressure cleaning equipment, the 150-200MPa high-pressure water washed through the stainless steel reactor nozzle dirt.

Second, the chemical cleaning: first of all to know the scale-like element within the device, it is best to sample analysis. After the dirt do first test to determine thecomposition, selection of cleaning agents also determined by experiments on the stainless steel reactor will not cause corrosion of metal equipment. Then loop through the field to set up temporary devices within the cleaning fluid circulating in the device,wash away the dirt.

    These two methods have advantages and disadvantages, chemical cleaning, less labor, cleaning time is short, thorough cleaning, but may cause corrosion of stainless steel reaction vessel equipment; mechanical cleaning equipment will not cause corrosion of stainless steel reactor, on the hard scale can be effectively cleaned,However, when using long, labor-intensive. Therefore, chemical cleaning applicationsin the dirt soft, thin condition, mechanical cleaning applications in the dirt hard, thickconditions. As for what should be the best option, it is necessary according to their specific situation.

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How to do Reactor Maintenance

Maintenance of reactor and other mechanical devices in addition to the conditions ofthe same note, there is attention to the following questions

1, in operation, reactor should be carefully checked for anything abnormal, in normal operation, the board shall open the cover and touch the terminals to avoid electric shock.
2, reactor the measuring instrument should be calibrated regularly to ensure accurate and reliable work.
3, the heating rate should not be too fast, slow pressure should be, especially the stirring speed, only slowly increases the speed. In case of power failure, should betransferred back to zero speed control knob.
4, no quick cooling to prevent excessive thermal stress damage.
5, reactor operation, the coupling between the lid and kettle water jacket cooling water must pass in order to control the operating temperature magnet, to avoiddemagnetization.
6, is strictly prohibited under high pressure tap screw bolt and nut connection.

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Keywords: reactor,pressure vessel,heat exchanger