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Precursor vaporizer systems

SIGA’s precursor evaporation systems enable the precise, carrier-free dosing and evaporation of liquid chemicals for CVD, PECVD, ALD and other deposition processes – safely, efficiently and cost-effectively.

We respond to our customers’ requirements, develop solutions in line with their specifications and tailor our systems to their needs.

Platform V107 / V108 precursor vaporizer for one precursor and one process outlet

Our precursor vaporizers, based on the "baking" principle, allow for the dosing of the correct amount of precursor without the use of a carrier gas. 

The V107/V108 base system comprises an evaporator with a rinse inlet and one process outlet. Various configuration options are available, such as dosing into a process gas stream and the mixing of different vapours and gases. Where required, features such as controlled inerting of the exhaust gas stream, pressure relief valves, gas sensors, ventilation systems, back-pressure regulators and other process-specific components can be added. 

There are now more than a dozen versions of the system, which we would be happy to tailor further to your requirements.

SIGA Precursor Verdampfer eiinfach RI Schema
Precursor Verdampfer V108
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The simplest V107/V108 precursor vapourisation systems allow the vapour to be metered using an MFC from a heated vessel. All pipework is located within a heated area to prevent condensation.

Feature
Data vaporizer system V107/V108 with one precursor
Dimensions H x W x D (mm)
1900; 600; 600
Delivery rate / throughput
typically 50 g/h to 2,000 g/h depending on the medium (continuous operation with refilling)
Evaporation temperature
Standard up to 55 °C, extended up to 90 °C, adaptable up to 140 °C Capacity
Capacity
3.5 l effective (5.2 l vessel)
Precursor chemicals (others available on request)
Silicon tetrachloride (SiCl₄), titanium(IV)-chloride (TiCl₄), trichlorosilane (HSiCl₃), hexamethyldisiloxane HMDSO (C₆H₁₈OSi₂), hexamethyldisilazane HMDS (C₆H₁₉NSi₂), chlorotrimethylsilane TMCS (C₃H₉ClSi), trimethylaluminium TMA (C₃H₉Al), diethylzinc DEZ (C₄H₁₀Zn), TEOS (C₈H₂₀O₄Si), titanium tetrachloride (TiCl₄), germanium- tetrachloride (GeCl₄), alcohols, water and much more.
Inert gas supply
100 Nl/h and 2–8 bar gauge pressure of nitrogen (N₂) or argon (purity 5.0 for chlorides 5.6), with inlet filter
Compressed air supply
5–8 bar g
Supply voltage
230 V / 16 A
Exhaust air for purging processes
approx. 5 l/min
Ex zones
No explosion-proof zones as the system is permanently technically leak-tight
Tightness
< 3E-8 mbarl/s helium, permanently technically leak-tight thanks to metallic face-seal fittings
Design
Enclosed cabinet with integrated, enclosed, heated evaporator compartment and independent, enclosed electrical cabinet.
Refilling
Connection for refilling during the process, refill trigger via scales, recommended refill system G504

Precursor vaporizer for a precursor and multiple process outlets 107/108-200

The ability to supply multiple consumers from a single evaporator makes it possible to build complex systems in a more compact manner and to utilise a shared evaporator source with the same medium. Overall, this reduces complexity and, consequently, costs and maintenance requirements, whilst increasing robustness.

Precursor Verdampfer mehrere Prozessausgänge RI Schema
Precursor Verdampfer mehrere Prozessausgänge
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Evaporator system, V107 variant, with 3 independent process outputs for metal alkyl evaporators.

Feature
Data vaporizer system V107/V108 with one precursor
Dimensions H x W x D (mm)
1900; 600; 600
Delivery rate / throughput
typically 50 g/h to 2,000 g/h depending on the medium (continuous operation with refilling)
Evaporation temperature
Standard up to 55 °C, extended up to 90 °C, adaptable up to 140 °C Capacity
Capacity
3,5 l effektiv (Behälter 5,2 g);
Precursor chemicals (others available on request)
Silicon tetrachloride (SiCl₄), titanium(IV)-chloride (TiCl₄), trichlorosilane (HSiCl₃), hexamethyldisiloxane HMDSO (C₆H₁₈OSi₂), hexamethyldisilazane HMDS (C₆H₁₉NSi₂), chlorotrimethylsilane TMCS (C₃H₉ClSi), trimethylaluminium TMA (C₃H₉Al), diethylzinc DEZ (C₄H₁₀Zn), TEOS (C₈H₂₀O₄Si), titanium tetrachloride (TiCl₄), germanium- tetrachloride (GeCl₄), alcohols, water and much more.
Inert gas supply
100 Nl/h and 2–8 bar gauge pressure of nitrogen (N₂) or argon (purity 5.0 for chlorides 5.6), with inlet filter
Compressed air supply
5–8 bar g
Supply voltage
230 V / 16 A
Exhaust air for purging processes
approx. 5 l/min
Ex zones
No explosion-proof zones as the system is permanently technically leak-tight
Tightness
< 3E-8 mbarl/s helium, permanently technically leak-tight thanks to metallic face-seal fittings
Design
Enclosed cabinet with integrated, enclosed, heated evaporator compartment and independent, enclosed electrical cabinet.
Refilling
Connection for refilling during the process, refill trigger via scales, recommended refill system G504
Precursor Verdampfer System V107G-051A Dimensions

Platform V111 precursor vaporizer system for two or more precursors to be mixed with process gases

If a separation process involves the separation of several components that are present as liquids and are mixed with process gases or metered alternately, this platform allows for the full range of combinations, whilst also enabling multiple process outputs to be managed. The example shows a system with 2 evaporators and 6 process outputs, each of which meters independently. The platform has been built on numerous occasions and can be further adapted.

The system can also be adapted to different process gases through the use of multi-range and multi-gas MFCs. 

By combining multiple components within a single system, it is possible to achieve a simply coordinated control system and to build a more compact system, which, taken together, reduces costs, maintenance requirements and integration efforts.

Internal connections improve reliability. MFC lines can be configured with redundancy to facilitate maintenance during continuous operation.

Precursor Verdampfer mehrere Prozessausgänge 2 RI Schema
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Precursor vaporizer system by
Charge & Release from buffer tanks

As an alternative to dosing via an MFC, defined quantities of vapour can also be dispensed quickly using the ‘charge and release’ method from buffer vessels. This is particularly useful when defined quantities need to be dispensed within a short time. The ‘charge and release’ method is a viable solution for both small quantities dispensed quickly (e.g. ALD) and large quantities dispensed quickly.

A set pressure is built up in the buffer vessel from the evaporator. Valves close off the path to the evaporator. As required, other valves open the path to the process chamber. The vapour then flows from the buffer vessel into the chamber. The volume of the buffer vessel and the change in pressure during discharge allow the precursor vapour to be metered in a reproducible manner. The pressure build-up in the buffer vessel can be controlled, and processes can be further varied by diluting the vapour with a carrier gas.

This offers a wide range of control options for achieving precise and stable dosing processes. As the process operates entirely without MFCs, this system can also handle temperatures in excess of 200°C.

Charge and Release System für ALD
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SIGA GmbH’s Charge & Release systems enable the controlled delivery of steam volumes and steam pulses without the need for an MFC.

Charge and Release System für ALD RI Schema
CharacteristicCharge and Release system for 1 or 2 precursors and 1, 2, or more buffer vessels
Dimensions H x W x D (mm)e.g. 2100 x 1600 x 850 / 1900 x 800 x 850
Delivery rate / throughputTypical process parameters: release of 1 mg to 5 g in 2 to 10 seconds; cycle time 10 s to 90 s.
Number of precursorsUp to 2 (more on request)
Number of process outletsBis 2 + X
Additional process gases1 + X e.g. nitrogen, H2, argon, silane
Evaporation temperaturePossible up to over 200°C (no MFC)
Evaporator capacity0.5 to 27 l possible
Buffer vessel capacity0.1 l to 30 l possible
Number of buffer vessels1 + X possible
Precursor chemicals (others available on request)Silicon tetrachloride (SiCl₄), titanium(IV)-chloride (TiCl₄), trichlorosilane (HSiCl₃), hexamethyldisiloxane HMDSO (C₆H₁₈OSi₂), hexamethyldisilazane HMDS (C₆H₁₉NSi₂), chlorotrimethylsilane TMCS (C₃H₉ClSi), trimethylaluminium TMA (C₃H₉Al), diethylzinc DEZ (C₄H₁₀Zn), TEOS (C₈H₂₀O₄Si), titanium tetrachloride (TiCl₄), germanium- tetrachloride (GeCl₄), alcohols, water and much more.
Inert gas supply100 Nl/h and 2–8 bar gauge pressure of nitrogen (N₂) or argon (purity 5.0 for chlorides 5.6), with inlet filter
Compressed air supply5–8 bar g
Supply voltage230 V / 16 A
Exhaust air for purging processesApprox. 5 l/min
Ex zonesNo explosion-proof zones as the system is permanently technically leak-tight
Leak tightness< 3E-8 mbarl/s helium, permanently technically leak-tight thanks to metallic face-seal fittings
SafetySafety temperature limiter, emergency stop function, spring-return valves in the event of a power failure or emergency stop, ventilation options, gas sensors
DesignEnclosed cabinet with a heated evaporator compartment and a heated buffer zone
RefillingConnection for refilling during the process, refill trigger via scales, recommended refill system G504
ControlControl via Beckhoff IPC via a local panel and remote interface. Configurable routines for: steam discharge, purging procedures, refilling process, manual mode for maintenance work
Control interfaceRemote HMI, Secure ADS, Profinet, RS485 supported. Triggering routines, reading sensor data, setting configuration values

Bubbler type precursor vaporizer

Precursor vaporization systems based on the bubbler principle utilize a carrier gas that is passed through the heated vaporization tank and exits the bubbler together with the precursor vapor.
They are particularly suitable for processes in which sufficient process pressure cannot be generated by the precursor vapor alone.

Am Eingang des Verdampfers wird der Fluss des Trägergases kontrolliert, während am Ausgang der Druck, sowie im Verdampfer die Temperatur gemessen wird. Als kostengünstige alternative zu trägergasfreien Verdampfern ist bei Bubbler-Verdampfersystemen eine geringe Verunreinigung des Precursers, durch das Trägergas hinzunehmen. Der Precursor enthält Rückstände des Trägergases, da der Precursor kontinuierlich mit dem Trägergas durchströmt wird.

Thanks to its design, the bubbler offers a highly cost-effective overall system for processes where moderate precision is sufficient.

To achieve lower loading rates and enable vaporization at temperatures below ambient, a secondary heat exchanger with a cooling unit can be employed.

Our basic system comprises a bubbler equipped with a carrier gas mass flow controller (MFC) at the inlet and a pressure control unit at the outlet.

We would be happy to configure your system to meet your specific requirements.

Precursor Verdampfer Bubbler
Precursor Verdampfer Bubbler
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Bubbler Precursor Verdampfersysteme der SIGA GmbH

CharacteristicBubbler type precursor vaporizer system
Dimensions H x W x D (mm)From 350 x 600 x 760
Delivery rate / throughputTypically up to 20 g/h; other rates depending on precursor available upon request.
Number of precursors1
Number of process outlets1 with branching
Carrier gasTypical N2 5.6, up to 2000 sccm
Evaporation temperatureBis 70°C, höhere Temperaturen auf Anfrage
Evaporator capacityCapacities from 0.5 to 27 L possible; suitable for standard containers such as DOCK10, 20, 50, or 100
Precursor chemicals (others available on request)Silicon tetrachloride (SiCl₄), titanium(IV)-chloride (TiCl₄), trichlorosilane (HSiCl₃), hexamethyldisiloxane HMDSO (C₆H₁₈OSi₂), hexamethyldisilazane HMDS (C₆H₁₉NSi₂), chlorotrimethylsilane TMCS (C₃H₉ClSi), trimethylaluminium TMA (C₃H₉Al), diethylzinc DEZ (C₄H₁₀Zn), TEOS (C₈H₂₀O₄Si), titanium tetrachloride (TiCl₄), germanium- tetrachloride (GeCl₄), alcohols, water and much more.
Inert gas supply100 Nl/h and 2–8 bar gauge pressure of nitrogen (N₂) or argon (purity 5.0 for chlorides 5.6), with inlet filter
Compressed air supply5–8 bar g
Supply voltage230 V / 16 A
Exhaust air for purging processesApprox. 5 l/min
Ex zonesNo explosion-proof zones as the system is permanently technically leak-tight
Leak tightness< 3E-8 mbarl/s helium, permanently technically leak-tight thanks to metallic face-seal fittings
SafetySafety temperature limiter, emergency stop function, spring-return valves in the event of a power failure or emergency stop, ventilation options, gas sensors
DesignEnclosed cabinet with a heated evaporator
RefillingConnection for refilling during the process, refill trigger via scales, recommended refill system G504
ControlControl via Beckhoff IPC via a local panel and remote interface. Configurable routines for: steam discharge, purging procedures, refilling process, manual mode for maintenance work
Control interfaceRemote HMI, Secure ADS, Profinet, RS485 supported. Triggering routines, reading sensor data, setting configuration values

Liquid dosing followed by evaporation
(direct evaporation)

Dosing using a carrier gas is the more precise alternative to using so-called DLI (Direct Liquid Injection) systems or CEM (Controlled Evaporation and Mixing) systems.
In this process, both the mass flow rate of the carrier gas and that of the precursor are controlled. The two media are then combined. The liquid is vaporised and transported together with the carrier gas. Various systems exist, some of which utilise the heated carrier gas stream itself to further vaporise any aerosol that has formed.

Thanks to precise fluid metering, DLI systems ensure the highest levels of accuracy in both the quantity and composition of the process gases supplied.

SIGA GmbH incorporates components from renowned manufacturers into its systems as required. Drawing on our experience and independence, we also combine various precursors and processes within a single system to meet specific customer requirements.

Example: 4-line mixing system

– Silane from a gas cabinet
– HMDSO from a DLI system without carrier gas
– TTIP from a DLI system with carrier gas
– TMA from a direct evaporator (baking)

Precursor Verdampfer mit verschiedenen Technologien
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An evaporator and gas mixing system that combines both direct evaporators and two DLI systems

CharacteristicExample combination for liquid dosing followed by evaporation
Dimensions H x W x D (mm)2100 x 780 x 300
Delivery rate / throughput300 sccm HMDSO, 2.5 g/min TTIP, 100 SCCM TMA, 120 sccm silane
Number of precursors3
Number of process outlets1
Carrier gasMax. 4000 SCCM Argon
Evaporation temperature50°C
Evaporator capacity0.7 l each
Precursor chemicals (others available on request)Trimethylaluminum TMA (C3H9Al), hexamethyldisiloxane HMDSO (C6H18OSi2), hexamethyldisilazane HMDS (C6H19NSi2), TTIP tetraisopropyl titanate (C12H28O4Ti), others possible
Inert gas supply100 Nl/h and 2–8 bar g nitrogen (N2) or argon 5.6/6.0
Compressed air supply5–8 bar g
Supply voltage230 V / 16 A
Exhaust air for purging processesApprox. 5 l/min
Ex zonesNo hazardous zones, as the system is permanently technically sealed and container changes are performed without opening the system.
Leak tightness< 3E-8 mbarl/s helium, permanently technically leak-tight thanks to metallic face-seal fittings
SafetySafety temperature limiter, emergency stop function, valves closing via spring force upon loss of power or emergency stop, ventilation options, smoke sensor for sealant component
DesignEnclosed cabinet with heated evaporator sections in 4 zones
RefillingConnection for refilling during the process, refill trigger via scales, recommended refill system G504
ControlControl via Beckhoff IPC via a local panel and remote interface. Configurable routines for: steam discharge, purging procedures, refilling process, manual mode for maintenance work
Control interfaceRemote HMI, Secure ADS, Profinet, RS485 supported. Triggering routines, reading sensor data, setting configuration values

Customised precursor vaporizer systems

We build your customized evaporator solution based on our modular system to meet your specific requirements. We are accustomed to—and look forward to—integrating new components and solutions to provide you with an optimal, efficient result, whether for a series-produced system or a one-off project.

Precursor Verdampfer induviduelle
Precursor Verdampfer kundenspezifisch
AI illustration based on an actual SIGA system image; errors may occur.

Your process, your system!

Precursor vaporizer

Precursor vaporizer systems are used to evaporate and meter liquid precursors that are fed into a CVD, PECVD or ALD deposition process as a gas phase. The evaporation and metering of the precursors takes place either via a system without a carrier gas, the direct evaporator or using a carrier gas.

Typical applications include the evaporation and metering of water, solvents, silanes, chlorides and metal alkyls such as SiCl₄, TiCl₄, SiHCl₃, HMDSO, DEZ, TMA or TEOS. Naturally, all other precursors can also be used; we are happy to assess the feasibility of specific precursors and operating ranges. The evaporation systems are frequently used in CVD, PECVD or ALD processes for gas-phase deposition, usually at reduced process pressures (LPCVD) or with plasma assistance (PECVD). Applications also arise at atmospheric process pressures, such as in flame hydrolysis (FHD) or plasma spraying processes.

Among the distinctive features of the evaporation systems are, in addition to the ability to evaporate without a carrier gas, the ability to supply multiple consumers from a single evaporator. It is possible both to supply several process chambers simultaneously and to feed precursor vapour into the process chamber at various points.

The ability to supply multiple consumers from a single evaporator reduces the number of components, control elements and the space required for installation compared with other designs. Overall, this helps to reduce the costs of maintenance, plant engineering and system integration. Another option is to integrate two evaporators into a single system with a shared control system.  

Precursor vaporizer Direct evaporation systems (baking)

The precursor is fed into a stainless steel tank, the evaporator, where it is regulated to the desired evaporation temperature. The resulting vapour phase is regulated to the set flow rate via a mass flow controller (MFC) and fed into the process. Additional gas streams can be adjusted and fed into the process, irrespective of the required amount of precursor.

Precursor Vaporizer - Bubbler type

Bubbler systems, on the other hand, utilise a carrier gas flow to deliver the precursor by passing the carrier gas through a reservoir vessel. These systems are simple in design and, when combined with standard containers (e.g. DOCK), provide a cost-effective, reproducible solution within a range of accuracy that is sufficient for many processes. The range of accuracy can be improved by using additional sensors. For example, a humidity sensor can be used in conjunction with a water evaporator to measure the humidity downstream of the bubbler. The required humidity level can be achieved by mixing in dry nitrogen (see AKF humidification stations).

Processes in which accuracy is of the utmost importance should, however, favour direct evaporator systems.

Precursor vaporizer DLI systems (Direct Liquid Injection)

DLI systems represent another variant. Here, the precursor is evaporated in a metered manner using a liquid flow controller and then mixed with the carrier gas. To enable evaporation at the level of the carrier gas pressure, the gas flow itself is utilised for aerosol formation and evaporation. Process temperatures range from room temperature to well over several hundred degrees Celsius. Owing to the independent flow control of the precursor and carrier gas, these systems achieve a high degree of accuracy in absolute dosing, similar to direct evaporators, but can reach higher maximum pressures.

Such equipment is available on the market from various manufacturers, and we at SIGA GmbH integrate it into our systems as required. However, this complex equipment makes the systems more expensive and must be operated using high-quality media, as replacing the components is considerably more costly than replacing a simple MFC.

Precursor vaporizer Charge & Release systems

Charge & Release systems dispense without the use of MFCs, based on pressure and volume in a buffer vessel. The buffer vessel is filled with vapour from the evaporator up to a maximum of the current evaporator pressure and then emptied into the process. The dispensed volume can be controlled via pressure differential, temperature and volume. These systems do not require MFCs and allow for the dispensing of small vapour volumes, as required in ALD processes, as well as the short-term delivery of high flow rates. By adjusting the pressure and temperature, as well as using buffer vessels and outlet orifices, reproducible processes can be set up across a wide range of parameters. Furthermore, the systems operate without being limited, for example, by the temperature resistance of MFCs.

Precursor vaporizer - SIGA GmbH

Siga GmbH is capable of designing and installing all types of evaporator systems. Furthermore, where appropriate, we also design combinations of different operating principles in order to achieve the optimal system or come as close to it as possible.

Our evaporator systems feature metal seals; elastomers are not used within the evaporator system. This fulfils a key requirement for safe operation. The system is designed on a bespoke basis according to the specific requirements of each application. The operating temperature of the evaporator is determined by the process pressure and the vapour pressure of the selected precursor and can, for example, range up to 80°C or up to 140°C.

Pressure and temperature within the evaporator are monitored; in the event of overpressure or overtemperature, the evaporator’s heating is switched off. All components carrying precursor vapour are heated. The system is housed in its own enclosure. Pipe trace heating for the vapour line to the process chamber is also fitted if the line pressure so requires.

The pipework and all components in contact with precursor vapour are made of stainless steel, material no. 1.4404, equivalent to SS316L. Face-seal fittings are used, e.g. Swagelok VCR. The utmost importance is attached to ensuring a leak-tight design. Fixed pipe joints are welded using orbital welding under an inert gas atmosphere.

The evaporator can be automatically refilled whilst the process is running. A precursor refill system is used to refill the evaporator. The precursor is stored in a storage vessel and, with the aid of a gas reservoir, is forced out through an immersion tube and fed into the evaporator.

The evaporator is controlled and monitored – including temperature control and automatic refilling – by the evaporator control system via a programmable logic controller (PLC) with a touch-screen for visualisation and operation. All functions are regulated by this control system. The setpoint for the MFCs and the selection of the desired gas path are determined by the higher-level control system of the coating plant. Communication is via a Profibus DP or another serial interface. The details of the control system, such as the type of operation with options for manual intervention and communication with the higher-level control system, are adapted to the requirements of the process.

The evaporator systems are installed in suitable sheet steel enclosures or in standard control cabinets. The control unit and evaporator can be integrated into a single cabinet or installed in two separate cabinets. The configuration can be adapted so that the system can be integrated into the coating plant as effectively as possible and tailored to the requirements at the installation site.

The integrated PLC control system with touch screen enables automatic regulation of temperature, pressure and level. Continuous replenishment whilst the process is running can be achieved via an external supply system with a gas reservoir – reliably and user-friendly. Communication with the main plant takes place via Profinet, Ethernet with SecureADS, RS485 or other industry standards.

In addition to passive safety elements and enclosed safety components such as safety temperature switches or safety threshold switches, a safety PLC (e.g. TwinSAF) is also used where necessary; this routes safety-critical functions and can interrupt or activate them independently of the actual control programme, based on a logic table derived from a safety assessment.

Safety functions such as shutdown in the event of overpressure or overtemperature are an integral part of the control system. The system can be configured modularly: as a stand-alone solution or as a multi-precursor system with central control. Enclosures made of sheet steel or in explosion-proof designs are available, as is integration into existing control cabinets.

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