A Bennaceur Arles

A Novel Architecture for Mobile Distributed Trie Hashing System

Keywords: Mobility, scalability, distributed data structure, trie hashing

Scalable and Distributed Data Structures (SDDS) are a class of data structures completely dedicated to distributed environments. They allow the management of large amounts of data while maintaining steady and optimum performances. Several families of SDDS have been proposed: LH*, RP*, DRT*, CTH*. None of these SDDS deals with the mobile environment. In this paper we present a novel architecture that uses a scalable and distributed data structure to manage insert/find/range query operations for mobile clients. We describe the design and the implementation of a mobile CTH* prototype. Our experimental results prove the validity of the design choices and show interesting access performances. The capabilities of the mobile CTH* platform offer new perspectives for high performance and ubiquitous data intensive applications.

Introduction

Scalable and Distributed Data Structures (SDDS) are new data structures designed for multicomputers (i.e. collections of autonomous workstations or PCs connected through a high-speed network) [START_REF] Litwin | Linear Hashing for Distributed Files[END_REF]. An SDDS file is organized into data buckets which are stored in specific nodes called servers. The number of servers dynamically scales with the file growth. Servers are accessed from independent and autonomous nodes called clients. Each client has its own image of how data is distributed. Since this image is not updated synchronously, the client may have an outdated image and make an addressing error i.e. contact a server which does not contain the required data. This server is able to forward the client's request to the correct server which sends an Image Adjustment Message (IAM) to the client. The information in the IAM does not necessarily make the image totally accurate, but at least it avoids repeating the same error twice [START_REF] Litwin | Linear Hashing for Distributed Files[END_REF]. There are many SDDS schemes which extend traditional data structures. Thus, There is those based on hashing techniques like LH* [16] and those based on trees like RP* [START_REF] Litwin | LH* -A Scalable Distributed Data Structure[END_REF]. More information can be found in [2]. CTH* (Distributed Compact Trie Hashing) is a scalable and distributed data structure which adapts a dynamic hashing method called trie hashing for distributed environments. Trie hashing (TH) is one of the fastest access methods to primary key ordered dynamic files [START_REF] Zegour | Trie hashing with the sequential representations of the trie[END_REF]. Nowadays, it is not sufficient to offer simple and fast access to a large volume of data. It is necessary to create an environment of mobility where the user can access the data and resources anywhere, anytime. Mobile end-user devices and wireless connection technologies allow for anytime, anywhere vision [START_REF] Litwin | RP* : A Family of Order-Preserving Scalable Distributed Data Structures[END_REF] and recent developments [START_REF] Kleinrock | Nomadicity: anytime, anywhere in a disconnected world[END_REF] show remarkable approaches toward mobile computing. However, these developments often face the problem of striving towards mobility in a rather isolated way. Mobile technologies are somewhat limited and these limitations are not expected to disappear in the near future. Thus, we argue that mobile information systems can reach their expected advantages and user acceptance only through integration with existing wired infrastructures, i.e the full value of mobile computing can only be achieved by taking advantages of a wired infrastructure such as reliability, availability, bandwidth, richness in capabilities in conjunction with the benefits of wireless technologies such as mobility, ad hoc connectivity or context awareness [START_REF] Frescha | Pervasive webaccess via public communication walls[END_REF][START_REF] Banavar | Software infrastructure and design challenges for ubiquitous computing applications[END_REF]. In this paper we present a novel architecture that extends a scalable and distributed data structure scheme toward mobile environments. Section 2 presents an overview of the main concepts and characteristics of distributed compact trie hashing. Section 3 describes the proposed architecture. Section 4 presents the performance study. Section 5 suggests some potential applications. Section 6 positions our work with related work, and finally, Section 7 concludes by underlining the main results and highlighting future research directions.

Distributed Compact Trie Hashing (CTH*) concepts

We recall here the principles of CTH* schemes as defined in [START_REF] De | Scalable Distributed Compact Trie Hashing[END_REF]. A CTH* file is stored on server computers (nodes), and is accessed by applications on client nodes. The file consists of records identified by primary keys. Keys are character strings of fixed maximum length with characters, called digits, from a finite alphabet. The digits are assumed to be lexicographically ordered. Hence the set of all possible keys is totally ordered. The smallest digit of the alphabet is ' ' and the largest is '|'. Non-key parts of records are not of interest in what follows so we will identify records by their keys. Records are stored in buckets with a capacity of b records; b >> 1. Buckets are numbered 0, 1, 2...N . Basically, there is one bucket of a file per server, although different servers may share files. Buckets are assumed to be in RAM. The file starts with bucket 0, and scales up with inserts, through bucket splits. Bucket addresses are mapped to the network addresses of the servers using physical allocation. The splitting and addressing rules of CTH* are based on those of compact trie hashing (CTH) [START_REF] Zegour | Trie hashing with the sequential representations of the trie[END_REF]. CTH [START_REF] Zegour | Trie hashing with the sequential representations of the trie[END_REF] is a variant of the well-known method TH (trie hashing). CTH represents the digital tree in a compact preorder sequential form to minimize the memory space necessary to represent the trie. The idea is to represent the links in an implicit manner to the detriment of maintenance algorithms slightly longer than those of the standard method. CTH consumes only three bytes per file bucket, which makes it possible to address some millions of records with a small memory capacity. Every split moves about half of the records in a bucket into a new bucket at a new server, appended to the file. The splits are triggered by bucket overflows. In CTH*, a bucket that overflows reports to a dedicated node called the coordinator. The coordinator uses a PAT (Physical Allocation Table) to find a new server. If such a server exists, it informs the overflow server which initiates the record transfer. The address a is defined by the CTH addressing algorithm [START_REF] Zegour | Trie hashing with the sequential representations of the trie[END_REF]. To avoid a hot spot, CTH* clients do not access the coordinator for the address computation. As for any SDDS, a CTH* client has therefore its own image of the file. For CTH*, this consists of a trie; |0 for a new client. These values may differ from one client to another. The client uses its image to calculate the address a for c while issuing a (point-to-point) request (a search of key c, an insert or a delete of a record). It then sends the request to server a . It might occur that a = a. Hence, every server s receiving a request first tests whether s = a. For this purpose, every server keeps its own trie. If the test fails, the server forwards the request to another server. The CTH* test and the forwarding algorithm is as follows :

• Use the server trie to calculate the address a of c

• if a = a then accept c

• forward c to server a

The forwarding process could a priori create many hops. The major property of CTH* is, however, that every request to a CTH* file is delivered to the correct address after at most four hops, [START_REF] De | Scalable Distributed Compact Trie Hashing[END_REF]. The server also sends a message back to the client, called an Image Adjustment Message (IAM). For CTH*, an IAM contains the trie part that will be changed. The client executes the IA algorithm. The result is a better image, with a trie closer to the actual values. Also, as long as there is no new split, the same addressing error cannot occur.

The system is initialized with only server 0 which has an empty bucket and (|0) tree i.e. all keys are mapped to server 0. We can have several logical servers for the same physical server.

Architecture

Messaging

When designing enterprise applications, for example, in a corporate intranet, the choice of transport method is fairly trivial. Application developers can choose whatever solution suits their needs the best, since typically there are no firewalls disturbing the data connections inside the intranet. When the enterprise application is meant to be accessed from outside the intranet, or as in this case, from a mobile device, the number of suitable transport methods is considerably reduced. Hypertext Transfer Protocol (HTTP) is an application-level, request-response type of protocol that was originally designed for transferring raw data, such as Web pages, across the Internet. Today the protocol is used for various other purposes as well. The current version of the protocol is HTTP/1.1 and, compared to the earlier version (HTTP/1.0), it contains more enhanced features. For example, the underlying Transmission Control Protocol (TCP) connections can now be utilized more efficiently. Two of these features are the support for persistent connections and pipelining. By specifying the HTTP header value Connection: keep-alive, the underlying TCP connection can be kept alive for the duration of more than one requestresponse pair. This feature is useful in many situations related to enterprise applications, since bandwidth is not wasted by unnecessarily opening multiple TCP connections (with multiple TCP handshake messages for each connection). With pipelining, multiple requests can be sent at once in a single TCP segment. In addition to these, HTTP/1.1 has incorporated transport compression of data types to further reduce the use of bandwidth. [START_REF] Raaikainen | Application requirements for middleware for mobile and pervasive systems[END_REF] There are a couple of properties that make HTTP an attractive choice. Through the success of the Web, HTTP has become a very widely used protocol and today practically every device that has network access supports it -including mobile devices. There are many ready-to-use commercial and free HTTP servers available on the market. Moreover, since HTTP traffic typically uses TCP port 80 or 8080, it can easily navigate through firewalls without any additional reconfiguration. These advantages led us to choose HTTP for communication between the mobile client and the fixed servers. The downside of HTTP is that despite the improvements in HTTP/1.1, it is still not the fastest protocol available. This is mainly due to the properties of TCP, such as the so-called slow start mechanism, and the fact that HTTP traffic has low priority in the routers along a network. This means that especially when the network is congested, HTTP traffic slows down considerably. Sockets are the oldest and, as a concept, probably the simplest form of communication between applications on different devices. We simply have to create an application on the server to listen to an appropriate port for incoming connections and then set up the client application to connect to that host and port. Naturally, if there is a firewall between the client and the server, we need to reconfigure it to pass the traffic of the application. There are two types of socket connections available; the socket connection can use either User Datagram Protocol (UDP) or Transmission Control Protocol (TCP). Both of these are available essentially in all networked devices. The difference here is that with TCP a connection is always made between the client and the server and the same connection is used for consecutive messages, whereas each UDP datagram contains the target and source addresses and is forwarded individually through the network. This means that TCP guarantees that the messages are delivered in correct order to the application -UDP does not even guarantee that the datagrams are delivered at all. On the other hand, establishing and tearing down the connections takes more time and generates a lot more traffic than merely sending a single datagram when needed. Thus, we use UDP sockets for communications in the local network; in addition, we have a dedicated flow control protocol for requests using UDP messages, if losses are unacceptable. Thus, CTH* servers manage two communication protocols: UDP for the messages coming from fixed clients, the other servers or the coordinator and HTTP for mobile clients' requests. In a typical client/server model it is the server's duty to be running and available at all times and the client's duty to initiate connections to the server whenever needed. This type of interaction is called the "pull" technology (the client effectively "pulls" information from the server whenever needed). If the resources on the mobile device allow it, the client application can be up and running as well and the connection can be kept alive all the time. However, the mobile client in our application must be accessed from a server to allow image adjustment messages; thus, we use an intermediate program (proxy) that we call preserver. This preserver intercepts the mobile clients' HTTP requests, codes them to the adequate format and finally transmits them using UDP sockets. When it receives the servers' answers, it transmits them to the suitable client. It keeps the HTTP connection alive until the client receives all the IAM and the response to its request. This strategy offers the flexibility of the HTTP in a mobile environment, the speed of UDP in a local environment and allows the server to process the requests of both fixed and mobile clients in the same way.

Server

A server is created empty, and listening for a bucket creation request. These requests may create several buckets from different SDDS files. The buckets are allocated using the Bucket Allocation Table (BAT). BAT contains the bucket address, size and the ID of its file. The bucket creation request comes from a client for a new file or from a server with a bucket to split. For the clients, the server is identified by its IP address and UDP port. A site can support multiple servers on different ports. The servers use multithread processing, Figure 2. Several threads take care of the processing, asynchronously and in parallel.

They communicate through queues and semaphore. The ListenThread receives a client's request, and puts it into a FIFO RequestsQueue and waits for the next request. A WorkThread, from a pool of such threads noted W orkT hread i (i = 1, .., N ) in Figure 2, wakes up. The number of active WorkThreads depends on the server load. The thread reads the next request in Re-questsQueue. It identifies the operation to perform. WorkThreads continues with the processing of the requested operation. Then, it puts the answer into the ResponsesQueue. Finally, the SendThread sends the server's responses. The creation of a new bucket or the splitting of an old one, are as follows. The latter case subsumes the former so we present only that one. Let S 0 be the splitting server, and let the S i be any server among M currently started, 1 ≤ i ≤ M . The split at S 0 is done as follows. First, S 0 sends the SplitRequest message with the requested bucket size to the coordinator. If there is a server S i that has enough space, the coordinator replies to S 0 and gives it the S i address. S 0 locates the middle key C m in its bucket and splits the bucket into two groups. One group, let it be G 1 , contains records with keys C > C m and their CTH sub-trie. The other group G 2 contains all the other records and their sub-trie. S 0 , sends G 2 to S i . It then updates its trie and data zones. Finally, S i creates the bucket with the received records and subtrie. The clients' requests in RequestsQueue received during the split are dealt with as usual once the split is over.

Fixed client

The CTH* client architecture is structured into three modules: send, reception and processing. They run in parallel, and are further structured as in Figure 3.

Mobile client

The CTH* client architecture is structured into two modules: send and the processing. They run in parallel, and are further structured as in Figure 4. The processing module, composed from WorkThreads, processes the application request and sends it to the servers. It puts the outgoing request into a FIFO queue. The SendRequest thread reads the queue. It builds the messages to the servers accordingly and sends them. The thread WorkThread can then treat other functions until it receives the answer to its request. It then finishes the treatment and returns the result to the interface thread which displays it. As a mobile device can manage many HTTP connections simultaneously, we use a set of SendThreads to treat HTTP connections.

Preserver

The preserver plays a mediator's role between the mobile client and the CTH* servers. When an HTTP request is received, the preserver creates a new thread that encodes and sends the message to the server using a UDP socket. If this server is the correct one, it transmits the answer to the preserver. In the case of an addressing error, the server transmits an IAM and forwards the request to another server s . If s is the correct server, it transmits the answer to the preserver, otherwise it forwards it and so on. The preserver must keep the HTTP connection alive during the request processing and disconnect only when all the IAMs and the response have been received. To conduct the performance analysis of our prototype implementation, we used an application which builds the CTH* file by inserting a large number of Figure 6: Average insertion time for a mobile device data elements. The application uses random data keys. Attached to each key is a data element which has a random size. Bucket capacities range from 250 to 2500 bytes. To test servers' scalability in a more efficient way, we use virtual servers on the same machine. Given the range of capacities, we then have files with between 3 and 50 buckets. This section only presents a selection of our experimental results. More results can be found in [START_REF] Bennaceur | Intégration d'un client mobile CTH*, mémoire d'ingénieur[END_REF]. Adding a mobile client maintains the performances of the fixed stations: same access time (< 1ms) and same load factor (%70). Figure 6 shows the average insertion time. The curve demonstrates that mobile CTH* is truly scalable since the average insertion time is constant (about 1.5 s) and independent from the number of insertions. Hence, the insertion time does not deteriorate for large data structure sizes. In addition, Figure 6 indicates that the insertion time decreases when many records are used. This is due to the increased parallelism as each client operates concurrently. However, it is greater than the average insertion time for a fixed client. This is due to the low bandwidth and the longer latency time which are inherent in mobile networks. Hence it should decrease if we use a more advanced packet-switched mobile network like 3G. We also study its performances with range queries. A range query is an operation which is sent by a client, in parallel, to select a group of servers and its execution at each server is mutually independent [START_REF] Litwin | RP*: A Family of Order-preserving Scalable Distributed Data Structures[END_REF]. Queries to all the file buckets are the most typical and we restrict our attention to these queries. We obtain the graph in Figure 6. Support for range queries is a major advantage of order preserving methods like RP* and CTH*.

Subsequently, it would be interesting to incorporate the latency periods experienced in practice when using different transmission technologies. Whereas test runs of the client on an emulator located on the same computer or in the same network as the server exhibit scarcely any differences among the protocols, such differences become truly noticeable with a GSM or even a GPRS link.

Some potential applications

The general requirements for enterprise applications are that they are scalable, can be run in heterogeneous environments, and their development and deployment cycles are as short as possible. These can be achieved by choosing the right architectural model and the right technology for the task at hand [START_REF]Enterprise: Developing End-To-End Systems[END_REF]. All these requirements apply to mobile applications as well. Most notably, the wireless environment is yet another piece in the puzzle of heterogeneous environments. As a rule, the mobile environment is much more restrictive than, for example, a normal corporate intranet environment as regard a how complex and heavy the client part of the application may be. Many enterprises already have a good selection of applications to which they might want to add access from company's mobile devices. To totally rewrite the applications would be a waste of time and resources. If possible, mobile client applications should be adapted to these existing applications and use existing code as much as possible. Some technologies are better than others for this purpose of acting as a wrapper over existing systems. If, on the other hand, the developer can make a clean start on both the client and the server side of the application, some other technology might be more suitable. Our main target was to provide a platform with a flexible protocol architecture that allows insert/find operations for mobile clients in a scalable manner. Examples of a typical application that would benefit from this platform might include database applications. Thus, we developed a sample application based on this platform. In our application scenario, different journalists take notes on their PDAs or cellular phones and transmit them instantly to the newspaper database. Every journalist can consult the notes of journalists working on the same topics. When returning to their office, they can find all the notes and start to write their articles. The primary purpose of this example is to provide an example application that uses our platform. Thus, the application has not been optimized in terms of user friendliness; it has been intentionally kept simple to maintain focus on the architecture itself. This framework inserts an additional security layer between the HTTP transport protocol and the application layer. When the mobile application starts and the user enters his or her name and password in the login screen, the application sends a login request to the preserver, which validates the user name and password and responds with either a login-OK or login-error response. While logged in to the server, the user can add new notes, update, search or delete old ones from different articles (groups of notes). He can also, create new articles. Due to wireless connection of the mobile device and the integration of the existing infrastructure, the user can access his database anywhere, anytime.

Related work

There is a lot of related work on SDDS, specially LH*. Many variants exist, such as LH*, LH* lh , variants that implement high availability (such as LH*s and LH* RS ) and also those adapted for P2P environments. They have been integrated into different DBMS, to provide self-managing and self-organizing data storage of potentially unbounded size. However, none of them deal with the mobile environment, which is of growing interest. We investigate this application area and take an important step towards implementing distributed data structures for mobile environments. Our architecture can be adapted to other SDDS like LH*. In addition, HTTP application request routing championed by Sarvega and subsequently by Cisco AON are examples of HTTP application requests from other computers. If one were to imagine HTTP requests from millions of handhelds, it is not clear that current hardware solutions can support them. We are proposing a novel scalable architecture. Whereas hardware solutions such as Sarvega (Intel) and AON (Cisco) can speed up the execution of an HTTP request routing, this method is the first approach to do something similar in a scalable fashion with online inserts. This paper has shown that even a software solution can get response times down to 1.5 seconds. This in conjunction with potential hardware solutions may be another interesting next step.

Conclusion

In this paper, we present a new mobile CTH* prototype which integrates fixed and mobile clients and offers simple, fast and efficient access to a great deal of information. It shows that scalable and distributed data structures can be ubiquitous. The object oriented design also gives this prototype more flexibility and extensibility. The experiments show that a client finds or inserts a given record in about 1.5 s. Among potential applications, we can cite modern database systems, continuously requiring larger scalable databases. Many existing databases or warehouses are growing extremely rapidly and require universal access. Further work, in progress, is extending our platform to include more aspects of mobile CTH* platform functionality. We are introducing mobile servers and adopting a peer-to-peer model. We are also optimizing the quantity of data exchanged between the mobile client and the preserver using compression methods and provide better security support using encryption methods. We are also managing high-availability using Reed Solomon codes [START_REF] Litwin | A High-Availability Scalable Distributed Data Structure using Reed Solomon Codes[END_REF][START_REF] Plank | A Tutorial on Reed-Solomon Coding for fault-Tolerance in RAID-like Systems, Software[END_REF].

Figure 1 :

 1 Figure 1: Global mobile CTH* platform Architecture

Figure 2 :

 2 Figure 2: Server's Architecture

Figure 3 :

 3 Figure 3: Fixed Client's Architecture

Figure 4 :

 4 Figure 4: Mobile Client's Architecture

Figure 5 :

 5 Figure 5: Preserver's Architecture

Acknowledgements

We would like to thank the anonymous reviewers for their valuable comments, which helped us improve the article.


Elisabeth Charlaix

Matteo Ciccotti
email: matteo.ciccotti@univ-montp2.fr

Klaus Sattler

Capillary Condensation in Confined Media

Keywords: capillary condensation, confined fluids, wetting, SFA, AFM

come

1 Physics of capillary condensation

Relevance in nano-systems

As the size of systems goes down, surface effects become increasingly important. Capillary condensation, which results from the effect of surfaces on the phase diagram of a fluid, is an ubiquitous phenomenon at nanoscale, occurring in all confined geometries, divided media, cracks, or contacts between surfaces [START_REF] Bowden | Friction and lubrication in solids[END_REF]. The very large capillary forces induced by highly curved menisci, have strong effect on the mechanical properties of contacts. The impact of capillary forces in Micro/Nano Electro-Mechanical Systems (MEMS & NEMS) is huge and often prevents the function of small scale active systems under ambient condition or causes damage during the fabrication process.

Since the nanocomponents are generally very compliant and present an elevated surface/volume ratio, the capillary forces developing in the confined spaces separating the components when these are exposed to ambient condition can have a dramatic effect in deforming them and preventing their service. Stiction or adhesion between the substrate (usually silicon based) and the microstructures occurs during the isotropic wet etching of the sacrificial layer (Bhushan et al 2003). The capillary forces cause by the surface tension of the liquid between the microstructures (or in the gaps separating them from the substrate) during the drying of the wet etchant cause the two surfaces to adhere together. Fig. 1 shows an example of the effect of drying after the nanofabrication of a nanomirror array. Separating the two surfaces is often complicated due to the fragile nature of the microstructures1 .

Figure 1: Stiction effect due to drying in the nanofbrication of a nanomirror array (c). The spacing between the lamellae is 200 nm as described in (a). If the aspect ratio of the lamellae is larger than a critical value, the stiffness of the lamellae becomes too small to withstand the attractive action of the capillary forces induced by drying at the moment where the liquid meniscus must bend to empty the interlamellar space. We remark that in drying processes the meniscus curvature and capillary pressure are quite smaller than the equilibrium values (cf. insert B), but they still have a great impact (Figure after Heilmann et al 2008).

In divided media, capillary forces control the cohesion of the media, but also have dramatic influence on the ageing properties of materials. Since the condensation of liquid bridges is a first order transition, it gives rise to slow activated phenomena that are responsible for long time scale variations of the cohesion forces (cf. section 2). Capillary forces also have a strong effect on the friction properties of sliding nanocontacts where they are responsible for ageing effects and enhanced stick-slip motion (cf. section 3). Finally, the presence of capillary menisci and nanometric water films on solid surfaces has deep consequences on the surface physical and chemical properties, notably by permitting the activation of nanoscale corrosion processes, such as local dissolution and recondensation, hydration, oxidation, hydrolysis, and lixiviation. These phenomena can either lead to the long term improvement of the mechanical properties of nanostructured materials by recrystallization of solid joints or to the failure of microsctructures due to stress-corrosion crack propagation (cf. section 4).

Physics of capillary condensation

Let us consider two parallel solid surfaces separated by a distance D, in contact with a reservoir of vapor at a pressure P v and temperature T . If D is very large, the liquid-vapor equilibrium occurs at the saturating pressure P v = P sat . For a finite D, if the surface tension γ sl of the wet solid surface (see insert A) is lower than the one γ sv of the dry solid surface, the solid favors liquid condensation. One should therefore ask if the solid can successfully stabilize a liquid phase when the vapor phase is stable in the bulk, i.e. P v < P sat . To answer this question, one must compare the grand canonical potential (see insert A) of two configurations: the 'liquid-filled interstice', which we shall call the condensed state, and the 'vapor-filled interstice', i.e. the non-condensed state: with µ = µ sat -∆µ the chemical potential of the reservoir. Outside of coexistence, i.e. if ∆µ = 0, the pressure in the two phases are different and are given by the thermodynamic relation ∂(P l -P v )/∂µ = ρ l -ρ v (with ρ l , ρ v the number of molecules per unit volume in each phase). As the liquid is usually much more dense and incompressible than the vapor the pressure difference reduces to (P v -P l )(µ) ≃ ρ l ∆µ = ρ l k B T ln(P sat /P v ) if the vapor can be considered as an ideal gas. Thus, the condensed state is favored if the confinement is smaller than the critical distance D c (µ):

ρ l ∆µD c (µ) = 2(γ sv -γ sl ) (1)
The left hand side of eq. ( 1) represents the free energy required to condense the unfavorable liquid state, and the r.h.s. the gain in surface energy. D c (µ) is thus the critical distance which balances the surface interactions and the bulk interactions to determine the phase diagram of the fluid [START_REF] Israelachvili | Intermolecular and surface forces[END_REF]). From the above equation it is clear that capillary condensation can occur only if the liquid wets, at least partially, the solid surfaces.

Insert A: Surface tension and contact angle

The surface tension of a fluid interface is defined in terms of the work required to increase its area

γ lv = ∂F ∂A lv N l ,V l ,Nv,Vv,T
Here F is the free energy of a liquid-vapor system, T its temperature, A lv the interface area, and N l , V l , N v , V v the number of molecules and the volume of each phase respectively [START_REF] Rowlinson | Molecular theory of capillarity[END_REF]. For a solid surface, one can likewise define a difference of surface tension γ sl -γ sv for the wet and dry surface in terms of the work dF required to wet a fraction dA sl of the surface initially in the dry state.

It is shown in thermodynamics that the surface tension is a grand canonical excess potential per unit area. The total grand canonical potential of a multiphase system:

Ω = -P v V v -P l V l -P s V s + γ lv A lv + (γ sl -γ sv )A sl
is the potential energy for an open system. Its variation is equal to the work done on the system during a transformation, and its value is minimal at equilibrium. On the diagram of insert B let us consider a horizontal translation dx of the meniscus. At equilibrium, the grand canonical potential is minimum: dΩ = -P l dV l -P v dV v + (γ sl -γ sv )dA sl = 0. Thus P v -P l = (γ sv -γ sl )/D. But, according to Laplace's law of capillarity, the pressure difference P v -P l is also related to the curvature of the meniscus: P v -P l = γ lv /r = 2γ lv cos θ/D, where θ is the contact angle. We deduce the Young-Dupré law of partial wetting:

γ lv cos θ = γ sv -γ sl valid if S = γ sv -γ sl -γ lv ≤ 0 (2)
The parameter S is the wetting parameter (de Gennes et al 2003). The situation S > 0 corresponds to perfect wetting. In this case a thin liquid layer covers the solid surface (see insert C).

In the case of partial wetting, the difference between the dry and wet surface tension is related to the contact angle θ of the liquid onto the solid surface and the critical distance reduces to

D c (µ) = 2γ lv cosθ ρ l ∆µ = 2r K cosθ (3)
where r K is the Kelvin's radius associated to the undersaturation ∆µ (see insert B).

For an estimation of the order of magnitude of the confinement at which capillary condensation occurs, consider the case of water at room temperature: γ lv = 72 mJ/m 2 , ρ l = 5.5×10 4 mol/m 3 , and assume a contact angle θ = 30 o . In ambient conditions with a relative humidity of P v /P sat = 40%, one has r k ≃ 0.6 nm and D c ≃ 1 nm. The scale is in the nanometer range, and increases quickly with humidity: it reaches 4 nm at 80% and 18 nm at 95% relative humidity. Therefore, capillary condensates are ubiquitous in ambient condition in high confinement situations.

Insert B: Laplace-Kelvin equation

Another way to address capillary condensation is to consider the coexistence of a liquid and its vapor across a curved interface. Because of the Laplace law of capillarity the pressure in the two phases are not equal: P int -P ext = γ lv /r, with r is the radius of mean curvature of the interface. The pressure is always higher on the concave side. Because of this pressure difference the chemical potential of coexistence is shifted :

µ v (P v ) = µ l (P l = P v -γ lv /r) = µ sat -∆µ
We have assumed here that the liquid is on the convex side, a configuration compatible with an under-saturation. For an ideal vapor and an uncompressible liquid:

∆µ = k B T ln(P sat /P v ) P l (µ) ≃ ρ l ∆µ + P v (µ) (4)
from where we get the Laplace-Kelvin equation for the equilibrium curvature [START_REF] Thomson | On the Equilibrium of Vapour at a Curved Surface of Liquid[END_REF]:

γ lv r K = P v (µ) -P l (µ) ≃ ρ l ∆µ = ρ l k B T ln P sat P v (5)
We check that in a flat slit, the critical confinement and the Kelvin's radius are related by D c = 2r K cosθ. The capillary condensate is thus limited by a meniscus whose curvature is equal to the Kelvin's radius. The Laplace-Kelvin law is however more general than eq.

(3) and allows to predict the critical confinement in arbitrarily complex geometries.

. We see from the Laplace-Kelvin equation that the pressure in capillary condensates is usually very low : taking the example of water in ambient conditions with relative humidity P v /P sat = 40%, the pressure in the condensates is P l = -120 MPa, i.e. -1200 bar. With these severe negative pressures, condensates exert strong attractive capillary forces on the surfaces to which they are adsorbed. Thus capillary condensation is usually associated to important mechanical aspects, such as cohesion, friction, elastic instabilities and micro-structures destruction. Furthermore, if the liquid phase wets totally the solid surfaces (see insert A), the surfaces may be covered by a liquid film even in a non-confined geometry (see inserts C and D). In this case the critical distance for capillary condensation can be significantly enhanced at low humidity. In the case of water, the condensation of a liquid film has important consequences on surface chemistry as surface species can be dissolved in the liquid phase, and the capillary condensation at the level of contact between surfaces increases solute transport and is responsible for dissolution-recrystallisation processes which lead to slow temporal evolution of materials mechanical properties (cf. sect. 4).

Mesoporous systems

Capillary condensation has been extensively studied in relation to sorption isotherms in mesoporous media -i.e. nanomaterials with pore sizes between 2 and 50 nm -in the prospect of using those isotherms for the determination of porosity characteristics such as the specific area and the pore size distribution. Fig. 3 for instance shows a typical adsorption isotherm of nitrogen in a mesoporous silica at 77 K. In a first domain of low vapor pressure, the adsorption is a function of the relative vapor saturation only, and corresponds to the mono-and polylayer accumulation of nitrogen on the solid walls. This regime allows the determination of the specific area, for instance through the Brunauer-Emmett-Teller model (1938). At a higher pressure a massive adsorption corresponds to capillary condensation, and the porous volume is completely filled by liquid nitrogen before the saturating pressure is reached. This adsorption branch shows usually a strong hysteresis and the capillary desorption is obtained at a lower vapor pressure than the condensation. This feature underlines the first order nature of capillary condensation. It is shown in the next paragraph that for sufficiently simple pore shapes the desorption branch is the stable one and corresponds to the liquid-vapor equilibrium through curved menisci. The desorption branch may be used to determine the pore size distribution of the medium through the Laplace-Kelvin relation using appropriate models (Barret-Joyner-Halenda 1951). More can be found on the physics of phase separation in confined media in the review of [START_REF] Gelb | Phase separation in confined systems[END_REF].

Insert C: Perfect wetting: the disjoining pressure When the energy of the dry solid surface γ sv is larger than the sum γ sl + γ lv of the solid-liquid and liquid-vapor interfaces (S > 0), the affinity of the solid for the fluid is such that it can stabilize a liquid film in equilibrium with an undersaturated vapor without any confinement. The existence of such wetting films must be taken into account when determining the liquid-vapor equilibrium in a confined space.

In the theory of wetting, liquid films are described by the concept of interface potential (Derjaguin 1955[START_REF] De Gennes | Wetting: statics and dynamics[END_REF]. The excess potential per unit area of a solid surface covered by a wetting film does not reduce to the sum γ sl + γ lv of the surface tensions: a further excess must be taken into account corresponding to the fact that the molecular interactions which generate the surface tension do not operate over a thickness of liquid that can be considered infinite. The excess grand canonical potential of the humid solid surface of area A is then

Ω sv A = γsv = γ sl + γ lv + W slv (e) -e(P l (µ) -P v (µ)) (6)
where the interface potential W slv (e) vanishes for a macroscopic film. The excess potential Ω sv /A describes the thermodynamic properties of the liquid film. It is minimum at equilibrium, so that the pressure in the liquid is not the same as in the vapor:

P v (µ) -P l (µ) = - dW slv (e) de = Π d (7)
The pressure difference Π d is called the disjoining pressure. The interface potential W slv (e) and the wetting parameter γsv (Π d ) -γ sl -γ lv are Legendre transforms of each other:

W slv (e) = γsv (Π d ) -γ sl -γ lv -eΠ d e = ∂γ sv ∂Π d (8)
For instance in the case of van der Waals forces, the interface potential results from dipolar interactions going as 1/r 6 between molecules, and varies as 1/e 2 :

W slv (e) = - A slv 12πe 2 Π d (e) = - A slv 6πe 3 γsv = γ sl + γ lv + -9A slv 16π 1/3 Π 2/3 d (9)
The Hamaker constant A slv has the dimension of an energy [START_REF] Israelachvili | Intermolecular and surface forces[END_REF]. It lies typically between 10 -21 and 10 -18 J and has negative sign when the liquid wets the solid, i.e. if the interface potential is positive.

Insert D: Perfect wetting: the prewetting transition and capillary condensation

In a situation of perfect wetting, a liquid film condenses on a flat isolated solid surface if the humid solid surface tension γsv is lower than the dry one:

γsv = γ sl + γ lv + W slv (e) + eΠ d ≤ γ sv (10)
If the film exists, its thickness at equilibrium with the vapor is implicitly determined by the analogue of the Laplace-Kelvin equation ( 5):

Π d (e) = - ∂W slv (e) ∂e = P v (µ) -P l (µ) = ρ l k B T ln P sat P v (11)
The thickness e * realizing the equality in relation ( 10) is a minimum thickness for the wetting film, and the associated chemical potential µ * and vapor pressure P * v correspond to a prewetting transition. Above the transition the thickness of the adsorbed film increases with the vapor pressure until it reaches a macroscopic value at saturation. In the case of van der Waals wetting for instance the vapor pressure at the prewetting transition is given by Π * d = ρ l k B T ln(P sat /P * v ) = 16πS 3 /(-9A slv ) with S the wetting parameter (2).

In a confined geometry such as sketched in Fig. 2, the grand canonical potential of the "non-condensed" state is shifted above the prewetting transition as the solid surface tension γ sv has to be replaced by the humid value γsv . The modified eq. ( 1) and the Laplace-Kelvin relation γ lv /r K = Π d = ρ l ∆µ give the critical distance [START_REF] Derjaguin | Polymolecular adsorption and capillary condensation in narrow slit pores[END_REF]:

D c = 2r K + 2e + 2 W slv (e) Π d (12)
The difference with the partial wetting case is not simply to decrease the available interstice by twice the film thickness. In the case of van der Waals forces for example,

D c = 2r K + 3e with e = (-A slv /6πρ l ∆µ) 1/3 (13)
The effect of adsorbed films become quantitatively important for determining the critical size for capillary condensation in a perfect wetting situation.

2 Capillary adhesion Forces

Measurements by SFA

Because of their high curvature, capillary condensates exert a large attractive force on the surfaces they connect. In return these large forces represent a valuable tool to study their thermodynamic and mechanical properties. Experimentally, the ideal geometry involves a contact with at least one curved surface -either a sphere on a plane, two spheres or two crossed cylinders -so that locally the topology resumes to a sphere of radius R close to a flat. Surface Force Apparatus (SFA) use macroscopic radius R in order to take advantage of the powerful Derjaguin approximation, which relates the interaction force F (D) at distance D to the free energy per unit area (or other appropriate thermodynamic potential) of two flat parallel surfaces at the same distance D (see insert E). It must be emphasized that the Derjaguin approximation accounts exactly for the contribution of the Laplace pressure, and more generally for all "surface terms" contributing to the force, but it does not account properly for the "perimeter terms" such as the line forces acting on the border of the meniscus, so that it neglects terms of order r K /R.

Insert E: Derjaguin approximation

Consider a sphere of macroscopic radius R at a distance D << R from a plane. If the range of the surface interactions is also smaller than R, then all surface interactions take place in the region were the sphere is almost parallel to the plane and the global interaction force F (D) is:

F (D) = - d dD ∞ D dA(z)[U(z) -U(∞)] = -2πR d dD ∞ D [U(z) -U(∞)]dz
with dA(z) ≃ 2πRdz the sphere area between altitude z and z + dz, and U(z) the appropriate potential energy per unit area for flat, parallel surfaces at distance z.

This gives the Derjaguin approximation :

F (D) = 2πR [U(D) -U(∞)]
In a surrounding condensable vapor the appropriate potential is the grand potential per unit area considered in Fig. 2:

Ω(D < D c ) = (ρ L -ρ v )∆µD + 2γ sl + W sls (D) Ω(D > D c ) = 2γ sv + W svs (D) (14)
with W sls (D) (resp. W svs (D)) the solid-solid interaction through the liquid phase (resp. vapor phase). This gives the interaction force in the case of partial wetting: and the pull-off force [START_REF] Fisher | Direct measurement of the effect of meniscus force on adhesion: a study of the applicability of macroscopic thermodynamis to microscopic liquid interfaces[END_REF] :

F (D < D c ) = 2πR -2γ lv cosθ + γ lv r K D + 2πRW sls (D) (15)
F pull-of f = -F (D = 0) = 4πRγ lv cosθ + 4πRγ sl = 4πRγ sv (16)
It should be mentioned here that the prefactor 4πR entering eq. ( 16) is valid only for rigid surfaces, i.e. if the Tabor parameter λ = (γ lv R 2 /E * 2 h 3 o ) 1/3 < 0.1 with E * the (mean) reduced Young modulus of the solid, and h o the range of the interaction. In the general case the 4πR prefactor in eq. ( 16) should be replaced by ǫ(λ)πR with 3 ≤ ǫ ≤ 4 [START_REF] Maugis | Adhesion of spheres: the JKR-DMT transition using a dugdale model[END_REF], Maugis et al 1993).

The pull-off force ( 16) is the sum of the capillary force 4πRγ lv cosθ and of the solid-solid adhesion in the liquid phase 4πRγ sl . A remarkable feature of eq. ( 16), valid in a partial wetting situation as we should recall, is that the capillary force does not depend on the volume of the liquid bridge nor on its curvature, a property due to the fact that the wetted area and the capillary pressure exactly compensate each other when the size of the condensate varies. Furthermore the pull-off force does not even depend on the presence of the condensate and is identically equal to its value in dry atmosphere, 4πRγ sv . Of course these remarkable results require a perfectly smooth geometry. In practice, even minute surface roughness screens very efficiently the solid-solid interactions, so that it can be neglected only in condensable vapor close to saturation. A major experimental problem is then to follow the transition of the pull-off force from 4πRγ sv to 4πR(γ lv cosθ + γ sl ) as the relative vapor pressure varies from 0 to 1. Surface Force Apparatus have addressed this problem using atomically smooth mica surfaces glued on crossed cylinders. However even with these physically ideal surfaces the pulloff force measured with dry surfaces gives a solid-solid surface tension γ sv significantly lower than the one obtained, for instance, from cleavage experiments or contact angle measurements [START_REF] Christenson | Adhesion between surfaces in undersaturated vapors-A reexamination of the influence of meniscus curvature and surface forces[END_REF]). The same occurs in liquid phase, where a monolayer of liquid remains stuck between the mica surfaces and prevents the measurement of the actual solid-liquid surface tension. Therefore a full experimental verification of eq. ( 16) over the whole vapor pressure range is not available. It is found however, that the pull-off force is dominated by the capillary force and that it does not depend on the vapor pressure over a significant range including saturation (cf. Fig. 4) [START_REF] Fisher | Direct measurement of the effect of meniscus force on adhesion: a study of the applicability of macroscopic thermodynamis to microscopic liquid interfaces[END_REF][START_REF] Christenson | Adhesion between surfaces in undersaturated vapors-A reexamination of the influence of meniscus curvature and surface forces[END_REF].

As the capillary force is less sensitive to roughness than the direct solid-solid adhesion (cf. insert H), SFA pull-off forces coupled to direct measurements of the Kelvin's radius via The attractive force varies linearly with the distance on a significant range where the condensate is at equilibrium with the vapor. For van der Waals forces the thickness e of the wetting film covering the surfaces is obtained through F cap (3e) = 4πRγ lv . It varies as the power 1/3 of the Kelvin's radius. Right: the pull-off force measured for various vapor pressures, and the comparison with the van der Waals dependence (19). The pull-off force is expected to saturate to the dry pull-off force at the prewetting transition.

the observation of the liquid bridge extension have been used to investigate the validity of the macroscopic capillarity at nano-scale, and an eventual drift of the liquid surface tension for highly curved menisci [START_REF] Fisher | Direct measurement of the effect of meniscus force on adhesion: a study of the applicability of macroscopic thermodynamis to microscopic liquid interfaces[END_REF]. The remarkable results is that the Laplace law of capillarity holds down to very small radii of curvature (i.e. less than 2-3 nm) for simple liquids. Discrepancies have been reported with water, but they have been shown to depend on the type of ions covering the mica surfaces, and have been attributed to the accumulation of involatile material in the water condensate [START_REF] Christenson | Capillary condensation in systems of immiscible liquids[END_REF][START_REF] Christenson | Adhesion between surfaces in undersaturated vapors-A reexamination of the influence of meniscus curvature and surface forces[END_REF]).

Valuable informations have been obtained by studying the full profile of the capillary force instead of only the pull-off force, as the slope of F (D) gives a direct measure of the Laplace pressure γ lv /r K . This requires however a SFA of large stiffness. Such analysis has been performed by Crassous et al (1993) in a perfect wetting situation. In this case the theoretical force is obtained from eq. ( 14) using the reference Ω(D = ∞) = 2γ sv instead of 2γ sv [START_REF] Charlaix | Adhesion forces between wetted solid surfaces[END_REF]:

F (D < D c ) = 2πR γ lv r K D + 2γ sl -2γ sv + 2πRW sls (D) (17)
The first term on the r.h.s. is the capillary force at liquid-vapor equilibrium. It also writes

F cap = 2πRΠ d (D -D c
) with D c given by eq. ( 12). Its slope provides the Laplace/disjoining pressure γ lv /r K = Π d , while the offset gives access to γsv and to the wetting potential with the help of eq. ( 8). Crassous et al verified experimentally eq. ( 17) down to Kelvin's radii of 3 nm in the case of heptane condensation on platinum surfaces.

A consequence of eq. ( 17) is to give the pull-off force as a function of the vapor saturation

F pull-of f = 4πRγ sv (18)
with γsv (Π d ) given by ( 8) and Π d by ( 11). For instance with van der Waals forces one expects:

F pull-of f = 4πR γ sl + γ lv + a ln P sat P v 2/3 (19)
with a = (-9A slv ρ 2 l (k B T ) 2 /16π) 1/3 . When the vapor pressure is increased from 0 to P * v , the pull-off force remains equal to the dry value 4πRγ sv . Above P * v the pull-off force decreases with increasing vapor pressure, until it reaches the wet limit 4πR(γ sl + γ lv ).

A major feature of capillary condensation is the strong hysteresis in the formation of the condensates. As shown on Fig. 5 for instance, the non-condensed state is highly metastable for D < D c , and an energy barrier has to be overcome to initiate the condensation process. The kinetics of capillary condensation has been much less studied than the static properties of the condensate. Several theoretical works have focused on the calculation of the energy barrier which depends on the confined geometry [START_REF] Restagno | Metastability and nucleation in capillary condensation[END_REF][START_REF] Lefevre | Intrusion and extrusion of water in hydrophobic mesopores[END_REF]. In the case of a wetting situation and of an extended slit like in SFA experiments, it has been shown that the distance of condensation D s (see Fig. 5) corresponds to the spinodal instability of the wetting film covering the solid surfaces [START_REF] Derjaguin | Polymolecular adsorption and capillary condensation in narrow slit pores[END_REF][START_REF] Christenson | Capillary condensation due to van der Waals attraction in wet slits[END_REF][START_REF] Crassous | Capillary condensation between highenergy surfaces: experimental study with a surface force apparatus[END_REF]. The growth kinetics of the capillary bridge after its initial formation has been shown by [START_REF] Kohonen | Kinetics of capillary condensation in a nanoscale pore[END_REF] to be reasonably well described by a model based on the diffusion-limited flow of vapor towards the bridge, except for water condensates which grow significantly more slowly; which is attributed to the effect of dissolution of inorganic material from the mica surfaces.

Measurements by AFM

The great relevance of capillary forces between nanoscale objects has stimulated the application of contact AFM to provide a more quantitative measurement of the forces acting between the very sharp probe tips (with typical radius of curvature of few nm) and samples with variable compositions or textures. The great advantage of AFM is the elevated lateral resolution, which is comparable with the curvature radius of the terminal portion of the probe tip. The first order effect of the probe size reduction is a proportional reduction of the adhesion forces to typical values in the nN range, which can easily be measured by AFM pull-off tests, i.e. by measuring the force of contact break down during a force-distance (approach-retract) curve. However, the typical cantilever stiffness (in the range of a few N/m) prevents the full characterization of the F (D) curve that can be obtained by SFA (cf. previous section), and typical data are limited to the variation of the pull-off force with relative humidity, corresponding to D = 0 [START_REF] Xiao | Investigation of humidity-dependent capillary force[END_REF].

Before entering a deeper analysis, we should remark that the AFM force measurements are very sensitive to many ill controlled factors, the more important being the exact details of the tip shape, including its nanoscale roughness. Although continuum derived laws become questionable at scales smaller than 1-2 nm, we will first establish how the capillary force at a finite distance D should properly be evaluated for nanoscale probes according to classical modeling and then discuss the limitations of this approach. Let the AFM tip be modeled as a cone terminating with a spherical tip of radius R and contact angle θ 1 and the sample as a flat surface of contact angle θ 2 (cf. Fig. 6). The Derjaguin approximation (insert E) leading to eqs. ( 16) and ( 18) is no longer applicable since the r K /R ratio is not negligible for nanoscale probes. Although other approximations exist, such as the circular meniscus surface model, their domain of validity is limited and their inattentive use can lead to severe errors. We thus recommend to refer to the complete analytical solutions provided by [START_REF] Orr | Pendular rings between solids-Menuscus properties and capillary force[END_REF], that describe constant mean curvature meniscus surfaces for systems amenable to a generic sphere/plane geometry (insert F), along with a computation of capillary forces. A special attention must be paid to the case of perfect wetting, since the Orr equations do not take into account the presence of wetting films. This situation was properly treated by Crassous (1995) using both an approximated solution and numerical simulation. In the case of a vanishing distance D, the solid-solid interactions should also be accounted for.

The capillary force F C acting on the sphere has two main contributions: a capillary pressure force F P , which is related to the negative Laplace pressure in the liquid bridge and acts on the sphere surface, and a surface tension force F S , which resides in the meniscus and acts on the contact line between the sphere and the liquid bridge. While this second term is negligible in the Derjaguin approximation, when R decreases to nanoscale its contribution becomes of the same order as the Laplace pressure term, since the ratio of the perimeter to surface of the capillary meniscus contact is increased. These terms can be written without any approximation as:

F C = F P + F S F P = -2πγHR 2 sin 2 ψ F S = 2πγR sin ψ sin(θ 1 + ψ) (20)
The filling angle ψ should then be related to relative humidity by using the Orr et al relations to evaluate the surface mean curvature (insert F) and by substituting it into the Laplace-Kelvin relation (5).

Insert F: Orr solutions for negative curvature menisci As observed by Plateau (1964), the meridian meniscus profile of a capillary bridge is expected to step through a series of shapes, including portions of nodoids, catenoids, unduloids, cylinders and spheres, as a function of the systems geometrical and wetting parameters. A clear report on the meniscus shapes as a function of the constant mean curvature can be found in Orr et al (1964), generally expressed in terms of elliptic integrals, as well as a characterization of the capillary forces that are the focus here. However, only nodoids are appropriate for describing capillary bridges equilibrated with undersaturated humidity, and catenoids are limited to the case of vanishing curvature (corresponding to saturated humidity or contact with a bulk liquid reservoir). We will thus only discuss here the case of a negative curvature. The mean curvature H = 1/2r K < 0 can be related to the parameters R, D, θ 1 , θ 2 and ψ by:

2HR/Ψ = Θ - 1 k [E(φ 2 , k) -E(φ 1 , k)] + 1 -k 2 k [F (φ 2 , k) -F (φ 1 , k)] (21)
where

Ψ = 1 D + 1 -cos ψ Θ = -cos(θ 1 + ψ) -cos θ 2 φ 1 = -(θ 1 + ψ) + π 2 φ 2 = θ 2 - π 2 k = 1 (1 + c) 1/2 c = 4H 2 R 2 sin 2 ψ -4HR sin φ sin(θ 1 + ψ)
and the functions F and E are the incomplete elliptic integrals of first and second type (Abramowitz and Stegun, 1972). Since the curvature H is present on both left and right hand terms of eq. ( 21), an iterative procedure is needed for numerical solution. The mean curvature H should then be related to the relative humidity through the Laplace-Kelvin relation (5). The contribution of capillary forces to the pull-off force can then be simply obtained by the taking the maximum value of the total force, which is obtained for D = 0.

However, the applicability of this subtle modeling to AFM pull-off force measurements is presently hampered by several technical problems. On the opposite of SFA, the shape of typical AFM probes is generally ill-defined and subject to easy degradation and contamination. Fig. 7 shows a typical example of pull-off force measurements as a function of humidity [START_REF] Xiao | Investigation of humidity-dependent capillary force[END_REF], along with the approximated modeling by de Lazzer et al (1999) aimed at showing the effect of a more general tip shape in the form of a revolution solid with radial profile y(x). Even if the considered tip profiles (cf. insert in Fig. 7) are quite similar, the modeled curves are quite different and can not account for the measured data. Although this modeling is based on the circular meniscus approximation and on an approximated estimate of the solid-solid van der Waals interactions, it can be retained as a clear proof of the critical effect of the tip shape on the capillary forces (cf. also Pakarinen et al 2005 for a less approximated modeling of the same data, leading to similar conclusions). It must be acknowledged that articles on adhesion measurements from the AFM community often do not show the same maturity as the SFA community in the subtle modeling of these phenomena, and thus often contain misleading interpretations that delay the establishment of a strong based modeling. The physical interpretation of AFM adhesion measurements in moist air still needs much work. The data in Fig. 7 can be considered as quite typical. The presence of a plateau at low humidity was often interpreted as the consequence of the non formation of a capillary bridge [START_REF] Xiao | Investigation of humidity-dependent capillary force[END_REF], reducing the adhesion force to the dry van der Waals solid-solid interaction. However, we showed in section 2.1 that no changes in the total adhesion force should be observed in the case of a vanishing meniscus between a perfect sphere and a plane in contact: even if the capillary bridge is strictly disappearing, the increased contribution of unscreened solid-solid interactions should strictly compensate the total adhesion force. The low humidity plateau could also be related to the effect of a small scale roughness in the tip and substrate (cf. insert H). At low humidity only the small contacting asperities would contribute to the pull-off force, and the rising regime is likely to be related to a transition towards a monomeniscus that may be treated according to the modeling presented in this section. More insights into the behavior at low humidity will be provided in section 3 by investigating the effect of capillary forces on cohesion and friction forces. The decreasing trend at higher humidity can be explained according to eq. ( 20): for small values of R (less than 1 µm), the increase of the meniscus section with humidity is not compensating any more the decrease of the Laplace pressure in the pressure term F P , due to the large values of the filling angle ψ . We remark that although the surface tension term F S is significantly increasing at elevated humidity, the decrease of the pressure term has a dominant effect on the total capillary force.

A major subject of open debate is the limit of validity of the continuum modeling at nanoscale, for both the capillary forces and their combination with the other relevant interactions such as van der Waals, electrostatic interactions, hydrogen bonding and other kinds of specific chemical interactions between the contacting tip and substrate. Although the capillary forces are generally dominant in the adhesion force (due the efficient screening of other interactions), this is not the case at low humidity where the solid-solid interactions become more relevant, especially for small radius probes. A notable example is given by the strong impact of electrostatic interactions in the adhesion force in dry atmosphere [START_REF] Wan | Fracture and contact adhesion energies of mica-mica, silica-silica, and mica-silica interfaces in dry and moist atmospheres[END_REF]. Although the continuum derived laws were shown to describe the adhesion forces in SFA measurements down to scales as small as 1-2 nm [START_REF] Lefevre | Intrusion and extrusion of water in hydrophobic mesopores[END_REF], the discrete nature and structure of solid and liquid molecules should become relevant at subnanometer scales, where the phase behavior of water is still debated. Several investigators have reported the complexity of the structure of thin water films, especially at low humidity where ice-like behavior is expected (cf. [START_REF] Verdaguer | Molecular structure of water at interfaces: wetting at the nanometer scale[END_REF]. Moreover, [START_REF] Xu | Wetting and capillary phenomena of water on mica[END_REF] have shown that the contact with an AFM tip can subtly modify the structure of the water layer on a mica substrate: 2D islands are left on the surface after removal of the tip and can persist several hours before evaporating. However, a significant disagreement is still found in literature on the details of the humidity dependence of these behaviors for different kinds of substrates and AFM tips and more accurate research is needed. In particular, the delicate role of non volatile material in water condensates should be carefully investigated.

Measurements in sharp cracks

Sharp crack tips in very brittle materials such as glasses have recently been proven to constitute an invaluable tool to study capillary condensation [START_REF] Grimaldi | The crack tip: a nanolab for studying confined liquids[END_REF]. By using a stable testing configuration such as the DCDC specimen it is possible to obtain extremely flat crack surfaces (with roughness of the order of 0.4 nm RMS on a 1x1 µm 2 region) and to induce a controlled crack opening profile by carefully loading the sample in pure mode I [START_REF] Pallares | Crack opening profile in DCDC specimen[END_REF]. We should highlight that although a nanometric roughness could be relevant affecting the capillary forces (cf. section 3), the complementarity of the roughness of brittle crack surfaces makes the local crack opening variations negligible. The crack opening 2u can thus be considered as a monotonously increasing function of the distance X from the crack tip. In a close neighborhood of the crack tip this can be expressed by a parabolic shape (cf. Fig. 8) according to the Irwin equation:

2u(X, K I ) = 2K I E ′ 8X π 1/2 (22)
where K I is the stress intensity factor and E ′ an effective Young modulus. The confinement in the sharp crack tips in glass is very elevated. Typical crack tip radii are of the order of 0.5 nm and the crack opening is of the order of 10 nm at 1 µm distance from the crack tip. This can be interpreted locally as a plane pore with progressive opening and it is thus expected to be filled with equilibrium capillary condensation up to a critical opening H c = D c (H c = 2r k cos θ for partial wetting and H c = 2r k +3e for perfect wetting under the assumption that the liquid-solid interactions are of the vdW type, cf. insert D).

Since the critical distance H c is generally in the nanometer range, the length L of the condensed phase is generally in the order of hundreds to thousands of nm and it has the advantage of significantly amplifying the effect of variations of H c . Accurate measurements of H c can be obtained by measuring the variations of the condensation length that are induced by a modulation of the crack opening profile through changes of the sample loading as shown in Figs. 8 and10. Such a measurement was recently made possible by the development of AFM phase imaging techniques (cf. insert G) that can detect the presence of capillary condensation in the crack cavity by measuring the energy dissipated in the formation of a liquid bridge between the condensed phase and the AFM tip during the imaging in tapping mode (Fig. 9).

Insert G: Capillary forces in AFM phase imaging (Tapping mode).

High amplitude oscillating AFM techniques (tapping mode) are widely used in surface imaging due to high lateral resolution and reduced tip and substrate damage. The cantilever oscillation is stimulated by a high frequency piezo driver at a constant frequency ω near the cantilever resonant frequency ω 0 (f 0 = ω 0 /2π ≃ 330 kHz) in order to have a free oscillation amplitude A 0 ≃ 30 nm at resonance. During the scan of a surface, a feedback loop acts on the vertical position of the cantilever in order to maintain the amplitude of the tip oscillation constant to a set point value A sp ≃ 20 nm. The vertical position of the cantilever motion provides the vertical topographic signal. Although the tip-sample interaction is non-linear, the motion of the tip can be well approximated by an harmonic oscillation z(t) = Acos(ωt+ θ). The phase delay θ between the stimulation and the oscillation of the cantilever can be related to the energy E diss which is dissipated during contact of tip and sample [START_REF] Cleveland | Energy dissipation in tapping-mode atomic force microscopy[END_REF]:

sin θ = ω ω 0 A sp A 0 + QE diss πkA 0 A sp ( 23
)
where Q ∼ 600 and k ∼ 40 N/m are the quality factor and the stiffness, respectively, of typical tapping cantilevers. Phase imaging can thus provide a map of the local energy dissipation caused by the tip-sample interaction during the cantilever oscillation. This quantity contains several contributions related to viscoelastic or viscoplastic sample deformation and also from the local adhesion properties. However, for very stiff substrates such as glass or silicon, the bulk dissipation will be negligible and phase imaging will mostly be sensitive to adhesion and in particular to the formation and rupture of capillary bridges between the tip and the sample at each oscillation. [START_REF] Zitzler | Capillary forces in tapping mode atomic force microscopy[END_REF] have developed a model to relate the energy dissipation to the hysteretic behavior of the capillary force-distance curve. In particular, it was shown that the formation of capillary bridges has a very sensitive influence on the position of the transition between attractive and repulsive modes in the tapping regime [START_REF] Ciccotti | Dynamic condensation of water at crack tips in fused silica glass[END_REF], and that this effect can be used to increase the sensitivity in the measurement of the local wetting properties.

On the other hand, capillary interactions can become a significant source of perturbation and artifacts in the topographical AFM images in tapping mode. Changes in the relative humidity during imaging can alter the stability of the mode of operation and induce an intermittent mode change which is the source of intense noise and local artifacts. In particular, in the presence of local patches with different wetting properties, the oscillation mode can systematically change between different areas of the image, inducing fake topographic mismatches. However, the topographical artifacts are of the order of the nanometer and are only relevant in very sensitive measurements on flat substrates. In such cases, an attentive monitoring of the phase imaging is required for detecting and avoiding the mode changes. Another drawback of the formation of capillary bridges is the significant loss of lateral resolution caused by the increase of the interaction area between tip and sample (cf. the smearing of the crack-tip condensate in Fig. 9). Again, a careful tailoring of the imaging conditions can lead the repulsive interaction to be dominant and thus allows recovering a higher resolution. The strongly negative capillary pressure in the crack cavity will apply important internal forces on the crack walls which add to the effect of the external forces and tend to close the crack. However, the advantage of such a stiff configuration is that even huge capillary pressures will have little effect on the crack opening profile when applied over a length L of micrometer size near the crack tip. The above cited technique can thus be comfortably applied to first order determinations of H c with 10% accuracy by neglecting the action of capillary forces. On the other hand, these forces can become more relevant if the external load (and thus the crack opening) are reduced enough to let the condensation extend to several tens of microns. In this context the deviations of the measured condensation length from the above cited prediction may be used to infer the value of the capillary pressure.

When implemented in controlled atmosphere, this technique can be used to measure both the critical condensation distance and the capillary pressure as a function of relative humidity and thus provide important information on the surface tension of the liquid, and on its Kelvin radius. This technique provides interesting complement to the SFA measurements since it does not suffer from the limitations of the SFA equipment to sustain the very strong negative pressures generated by the capillary meniscus at low humidity.

We remark that the values of the measured critical distance H c for water condensation in silica glass in Fig. 10 are quite large in relation to the prediction of eq. ( 13), which should not exceed 3 nm at 70% RH. This phenomenon of enhanced condensation is analog to other similar observations, such as the measurement of large meniscus radii in SFA measurements between mica sheets [START_REF] Christenson | Capillary condensation in systems of immiscible liquids[END_REF] where capillary bridges of water condensed from a non polar liquid were argued to be enriched by ionic solute. These interesting effects still need more investigation and will provide important information on the chemical effects due to glass water interactions under tensile stress (cf. section 4).

3 Influence on Friction forces

Static friction and powder cohesion

It is an everyday experience that a small amount of liquid can change drastically the physical properties of granular matter. Such effects are important not only on the beach for building sandcastles, but also in a number of industries as diverse as pharmaceutical, construction and agriculture, and in a number of geophysical applications. The changes induced by a small amount of liquid in granular materials are primarily caused by adhesive forces associated with interstitial liquid bridges between grains (Zimon 1967[START_REF] Bocquet | Physics of humid granular media[END_REF]. In the absence of cohesion forces the stability of a heap of beads can be described by a modified Mohr-Coulomb analysis, thus predicting a maximum angle of stability θ m = φ, where µ = tanφ = τ /σ is the static friction coefficient between the beads. The effect of an adhesive stress c between the beads can be modeled by writing a modified Coulomb yield criterion τ = µ(σ+c) and thus obtaining an implicit equation for the critical angle θ m [START_REF] Halsey | How sandcastles fall[END_REF]:

tan θ m = tan φ 1 + c ρgh cos θ m (24)
where ρ and h are the density and height of the granular layer. The critical angle is thus an increasing function of the adhesive stress c and it saturates to π/2 (stuck heap) when µc > ρgh.

Several experiments have recently been investigating the applicability of this relation and the consistency of the model with capillarity based adhesion forces. A first series of experiments has shown that the injection of a very small fixed amount of non volatile liquids to a granular heap can significantly increase the critical angle of stability (Hornbaker et al 1997, Halsey and[START_REF] Halsey | How sandcastles fall[END_REF]. A different kind of experiments has then investigated the more subtle effect of interparticle liquid bridges formed by condensation from a humid atmosphere [START_REF] Bocquet | Moisture-induced ageing in granular media and the kinetics of capillary condensation[END_REF][START_REF] Fraysse | Humidity effects on the stability of a sandpile[END_REF]. While the first kind of experiments can not be related to equilibrium quantities, the second kind has allowed a deep investigation of the first order transition of capillary condensation.

The critical angle was shown to be logarithmically increasing function of the aging time t w (after shaking) of a granular heap [START_REF] Bocquet | Moisture-induced ageing in granular media and the kinetics of capillary condensation[END_REF]:

tan θ m = tan θ 0 + α log 10 t w cos θ m (25)
The coefficient α is a measure of the aging behavior of friction in the granular medium and it was shown to be an increasing function of relative humidity, being substantially null in dry air. Moreover, the aging behavior was shown to be enhanced by both increasing the rest angle of the heap during the aging period and by intentionally wearing the particles (by energetic shaking) before the measurements [START_REF] Restagno | Aging in humid granular media[END_REF].

The logarithmic time dependency of the adhesion forces was modeled as an effect of the dynamic evolution of the total amount of condensed water related to progressive filling of the gaps induced by the particle surface roughness (cf. insert H). The increase of the aging rate α with the rest angle before the measurements can be explained by the effect of a series of small precursor beads adjustments, inducing a modification of the contacts and of the condensed bridges population. The effect of wear of the particles can be explained by accounting for both the increased roughness of the beads and the presence of a wear induced dust consisting in small particles that significantly enhance the nucleation of further bridges [START_REF] Restagno | Aging in humid granular media[END_REF].

Time and velocity dependence in nanoscale friction forces

Sliding friction is an everyday life issue, and its universal nature emerges from the great variety of industrial processes and natural phenomena in which it plays a central role (Persson 2000). With the miniaturization of moving components in many technological devices, such as microelectromechanical systems and hard disks, it has become of primary importance to study surface forces like friction, viscous drag and adhesion at microcales and nanoscales. The relevance of surface forces is greatly enhanced with regard to volume forces when the spatial scale is reduced to nanometers, but another major physical change comes from the increasing role of thermal fluctuations in the surface processes.

AFM has become the most efficient tool to study surface forces at the nanoscale, and the AFM tip sliding on a surface can often be considered as a model system for technologically relevant devices. The terminal apex of typical AFM tips can be roughly approximated by a sphere of radius between 10 and 100 nm, and the AFM contact imaging of a nanoscale rough surface can provide both a measure of its roughness through the vertical deflection of the probe cantilever and a measure of the friction forces through the dependence of the lateral deflection of the cantilever on the scan speed and on the normal applied load.

Nanoscale friction was rapidly shown not to respect the Amonton laws, being dependent on both sliding velocity and normal load. Moreover, it was shown to be strongly affected by the nanoscale roughness of the substrate and by the wetting properties of both the AFM tip and the substrate as well as by relative humidity. Nanofriction measurements have long been controversial, but recent careful measurements in controlled atmosphere have allowed defining a clearer scenario.

The sliding kinetics of an AFM tip has been shown to be determined by both the thermally activated stick-slip dynamics of the AFM tip on the substrate and the time dependent formation of capillary bridges between the tip and the asperities of the rough substrate (cf. insert H).

H. Effect of roughness on adhesion forces.

The first order effect of roughness is to screen the interactions between surfaces, with an increased efficiency for the shorter range interaction. The molecular range solid-solid interactions are thus very efficiently screened by nanoscale roughness, while the capillary interactions have a more subtle behavior. Three main regimes were identified by [START_REF] Halsey | How sandcastles fall[END_REF] as a function of the volume of liquid V available for the formation of a capillary bridge between two spheres: (1) the asperity regime prevails for small volumes, where the capillary force is dominated by the condensation around a single or a small number of asperities; (2) the roughness regime governs the intermediate volume range, where capillary bridges are progressively formed between a larger number of asperities and the capillary force grows linearly with V (as in Hornbaker et al 1997); (3) the spherical regime where eq. ( 16) for the force caused by a single larger meniscus is recovered. The extension of the three domains is determined by the ratio between the characteristic scales of the gap distribution (height l R and correlation length ξ) and the sphere radius R. When dealing with capillary bridges in equilibrium with undersaturated humidity, the roughness regime should be reduced to a narrow range of humidity values such that l R ∼ r k , in which the capillary force jumps from a weak value to the spherical regime value (as in the experiments of [START_REF] Fraysse | Humidity effects on the stability of a sandpile[END_REF]. However, due to the first order nature of capillary condensation transition, the equilibrium condition may be preceded by a long time dependent region where the capillary bridges between asperities are progressively formed due to thermal activation. The energy barrier for the formation of a liquid bridge of volume v d ∼ hA between asperities of curvature radius R c may be expressed as [START_REF] Restagno | Metastability and nucleation in capillary condensation[END_REF]:

∆Ω = v d ρ l ∆µ = v d ρ l k B T log P sat P v
The probability that condensation occurs before a time t w is:

Π(t w ) = 1 -exp - t w τ τ = τ 0 exp ∆Ω k B T
By integrating over a roughness dependent distribution of N tot nucleation sites, each one contributing with a force 2πγR C , an expression for the total force can be derived [START_REF] Bocquet | Physics of humid granular media[END_REF] that predicts a logarithmic increase as a function of the aging time t w :

F C = F 0 + 2πγR c N tot k B T V 0 ρ l ∆µ log t w τ 0 (26)
where V 0 is a roughness dependent range for the distribution of the individual liquid bridge volume v d .

When relative humidity is low, or the substrate is weakly wettable, stick-slip sliding has a dominant effect and results in a positive logarithmic dependence of the friction force on the sliding velocity (Gnecco et al 2000[START_REF] Riedo | Interaction potential and hopping dynamics governing sliding friction[END_REF]. The AFM tips keeps being stuck on nanoscale asperities and intermittently slips when thermal fluctuations allow skipping a local energy barrier which is progressively reduced by the accumulation of elastic energy due to the scanning. The dynamic friction force can be described by the following equation:

F F = µ(F N + F SS ) + µ[F c (t)] + m log v v B ( 27
)
where F N is the normal force, F SS the solid-solid adhesion force within the liquid, F c (t) describes the eventual presence of time dependent capillary forces and the last term describes the positive velocity dependence induced by stick-slip motion. For more hydrophilic substrates, higher relative humidity, or increasing substrate roughness, the formation of capillary bridges and wetting films deeply modifies the friction dynamics letting the friction force be a logarithmically decreasing function of the sliding velocity [START_REF] Riedo | Kinetics of capillary condensation in nanoscopic sliding friction[END_REF]. This effect was successfully explained by applying the modeling developed by Bocquet et al (1988) to account for the time dependent thermally activated formation of capillary bridges between the nanoscale asperities of both the probe and the substrate. When the two rough surfaces are in relative sliding motion, the proximity time t w of opposing tip and substrate asperities is a decreasing function of the sliding velocity v. The number of condensed capillary bridges (and thus the total capillary force) is thus expected to be a decreasing function of the sliding velocity according to eq. ( 26), and this trend should be reflected in the dynamic friction force according to eq. ( 27).

The study of AFM sliding friction forces has thus become an important complementary tool to study the time and load dependence of capillary forces. Notably, the friction forces were shown to present a 2/3 power law dependence on the applied load F N [START_REF] Riedo | The 2/3 power law dependence of capillary force on normal load in nanoscopic friction[END_REF] and an inverse dependence on the Young modulus E of the substrate [START_REF] Riedo | Interaction potential and hopping dynamics governing sliding friction[END_REF]. These two effects were both explained by the increase of the nominal contact area where capillary bridges are susceptible to be formed, when either the normal load is increased, or the Young modulus of the substrate is decreased. The following equation for the capillary force during sliding was proposed in order to account for all these effects:

F c = 8πγ lv R(1 + KF 2/3 N ) 1 ρ l l R R 2 c log v 0 v log Psat Pv K = 1 r K 9 16RE 2 1/3 (28)
the variables being defined as in the insert H. Quantitative measurements of the AFM friction forces were thus shown to be useful in determining several physical parameters of interest, such as an estimation of the AFM tip radius and contact angle or important information on the activation energy for the capillary bridge formation [START_REF] Szoskiewicz | Nucleation time of nanoscale water bridges[END_REF].

The formation of capillary bridges can have significant effects on the AFM imaging in contact mode due to the variations of the contact forces and consequently of the lateral forces during the scan. [START_REF] Thundat | Role of relative humidity in atomic force microscopy imaging[END_REF] have investigated the effect of humidity on the contrast when measuring the atomic level topography of a mica layer. The topographic contrast is shown to decrease with humidity above 20% RH due to an increase of the lateral force that acts in deforming the AFM cantilever and thus influences the measurement of the vertical deflection.

Friction forces at macro scale

Capillary forces can also affect the friction properties between macroscopic objects. In dry solid friction, ageing properties have been studied on various materials, and have been related to the slow viscoplastic increase of the area of contact between asperities induced by the high values of the stress in the contact region [START_REF] Baumberger | Physical analysis of the state-and rate-dependent friction law. II. Dynamic friction[END_REF]. However, the importance of humidity has been reported by geophysicists in rock onto rock solid friction [START_REF] Dieterich | Effect of humidity on time-dependent and velocitydependent friction in rocks[END_REF].

In the presence of a vapor atmosphere, the static friction coefficient was shown to increase logarithmically with the contact time, while the dynamic friction coefficient was shown do decrease with the logarithm of the sliding velocity [START_REF] Dieterich | Effect of humidity on time-dependent and velocitydependent friction in rocks[END_REF]. The first effect is analog to the aging behavior of the maximum contact angle in granular matter as discussed in section 3.1. The second effect is analog to what observed in the sliding friction of a nanoscale contact as discussed in the previous section. However, the general behavior is strongly modified due to the greater importance of the normal stresses that induce significant plastic deformation at the contact points. The aging behavior must then be explained by the combined action of the evolution of the contact population due to plastic deformation and the evolution of the number of capillary bridges due to thermally activated condensation. This induces a more complex dependence on the normal load, since this modifies both the elastic contact area and the progressive plastic deformation of the contacts, and thus influences the residual distribution of the intersurface distances that govern the kinetics of capillary condensation.

Based on these experimental observations, [START_REF] Rice | Stability of steady frictional slipping[END_REF] have proposed a phenomenological model for non stationary friction, in which friction forces depend on both the instantaneous sliding velocity v and a state variable ϕ according to:

F (v, ϕ) = F N µ 0 + A log v v 0 + B log ϕv 0 d 0 (29) φ = 1 - vϕ d 0 ( 30
)
where A and B are positive constants, while d 0 and v 0 are characteristic values of the sliding distance and velocity. The first term accounts for the logarithmic dependence on the sliding velocity, while the second term accounts for the logarithmic dependence on the static contact time through the evolution of the state variable ϕ according to eq. ( 30). This phenomenological modeling can be applied to other intermittent sliding phenomena (peeling of adhesives, shear of a granular layer, etc.) and the significance of the state variable ϕ is not determined a priori. However, in the case of solid friction, the state variable ϕ can be related to the population of microcontacts and capillary bridges [START_REF] Dieterich | Direct observation of frictional contacts-new insights for state-dependent properties[END_REF].

Influence on Surface Chemistry

The presence of nanometric water films on solid surfaces has deep consequences on the surface physical and chemical properties. Chemistry in these extremely confined layers is quite different than in bulk liquids due to the strong interaction with the solid surface, to the presence of the negative capillary pressure, to the reduction of transport coefficients and to the relevance of the discrete molecular structure and mobility that can hardly be represented by a continuum description. The role of thermal fluctuations and their correlation length also become more relevant.

Thin water films can have a major role in the alteration of some surface layer in the solid due to their effect on the local dissolution, hydration, oxidation, hydrolysis, and lixiviation which are some of the basic mechanisms of the corrosion processes. Water condensation from a moist atmosphere is quite pure and it is thus initially extremely reactive towards the solid surface. However, the extreme confinement prevents the dilution of the corrosion products, leading to a rapid change in the composition and pH of the liquid film. Depending on the specific conditions this can either accelerate the reaction rates due to increased reactivity and catalytic effects, or decelerate the reaction rate due to rapid saturation of the corrosion products in the film. This condition of equilibrium between the reactions of corrosion and recondensation can lead to a progressive reorganization of the structure of the surface layer in the solid. The extreme confinement and the significance of the fluctuations can cause the generation of complex patterns related to the dissolution-recondensation process, involving inhomogeneous redeposition of different amorphous, gel or crystalline phases (Watanabe et al 1994, Christenson and[START_REF] Christenson | Growth of ionic crystallites on exposed surfaces[END_REF].

The dissolution-recondensation phenomenon also happens at the capillary bridges between contacting solid grains or between the contacting asperities of two rough solid surfaces. When humidity undergoes typical ambient oscillations, capillary bridges and films are formed or swollen in moist periods, inducing an activity of differential dissolution. The subsequent redeposition under evaporation in more dry conditions is particularly effective in the more confined regions, i.e. at the borders of the solid contact areas, acting as a weld solid bridge between the contacting parts (cf. Fig. 11). This can be responsible of a progressive increase in the cohesion of granular matters, which has important applications in the pharmaceutical and food industry, and of the progressive increase of the static friction coefficient between contacting rocks. Another domain where the formation of capillary condensation has a determinant impact on the mechanical properties is the stress-corrosion crack propagation in moist atmosphere (cf. Ciccotti 2009 for a review). We already mentioned in section 2.3 that the crack tip cavity in brittle materials like glass is so confined that significant capillary condensation can be observed at its interior. During slow subcritical crack propagation, the crack advances due to stress-enhanced chemical reactions of hydrolysation and leaching that are deeply affected by the local crack tip environment. Capillary condensation has a fundamental impact on several levels on the kinetics of this reaction: (1) the presence of a liquid phase makes the preadsoprion of water molecules near the crack tip easier; (2) the negative Laplace pressure determines the chemical activity of the water molecules in the meniscus and directly affects the reaction rate; (3) the confined nature of the condensation along with its limited volume are responsible of an evolution of the chemical composition of the condensate that has a direct and major effect on the corrosion reactions at the crack tip, especially by changes of the pH and by the enrichment in alkali species due to stress-enhanced leaching [START_REF] Célarié | Stress-enhanced ion diffusion at the vicinity of a crack tip as evidenced by atomic force microscopy in silicate glasses[END_REF].

Figure 2 :

 2 Figure 2: Ω non-condensed (µ) = 2Aγ sv -DAP v (µ) Ω condensed (µ) = 2Aγ sl -DAP l (µ)

Figure 3 :

 3 Figure 3: Sorption isotherm of nitrogen at 77 K in Vycor (data from Torralvo et al 1998, A.Q. = adsorbed quantity).

Figure 4 :

 4 Figure 4: Mesured pull-off force as a function of the relative vapor pressure of cyclohexane. The dashed line is the bulk surface tension of cyclohexane (γ lv = 25 mN/m; data after Christenson 1988).

Figure 5 :

 5 Figure 5: Left: the capillary force between platinum surfaces measured in n-heptane vapor.The attractive force varies linearly with the distance on a significant range where the condensate is at equilibrium with the vapor. For van der Waals forces the thickness e of the wetting film covering the surfaces is obtained through F cap (3e) = 4πRγ lv . It varies as the power 1/3 of the Kelvin's radius. Right: the pull-off force measured for various vapor pressures, and the comparison with the van der Waals dependence (19). The pull-off force is expected to saturate to the dry pull-off force at the prewetting transition.

Figure 6 :

 6 Figure6: Graphical representation of a capillary bridge formed between an AFM tip of radius R and a flat surface separated by a distance D. ψ is the filling angle, r 1 and r 2 are the principal radii of curvature of the meniscus, θ 1 and θ 2 are the contact angles of the AFM tip and surface.

Figure 7 :

 7 Figure 7: Adhesion force (pull-off) measurements between a Si 3 N 4 AFM tip and a SiO 2 surface (circles). The theoretic approximated expressions calculated from the equations of de Lazzer et al (1999) are also shown for the three different tip shapes with radial profile y(x) represented in the insert (overlapping for x < 10 nm): (a) parabolic profile y = k 1 x 2 , (b) y = k 2 x 2.5 , and (c) more complex dull shape (Figure after Xiao and Qian 2000).

Figure 8 :

 8 Figure 8: Sketch of the variation of the condensation length after an increase of the stress intensity factor K I : (top) case of equilibrium; (bottom) constant volume model. NB: exaggerated vertical scale.

Figure 9 :Figure 10 :

 910 Figure 9: Typical AFM height (a) and phase (b) images of the crack tip for a fracture propagating from top to bottom of the image (1x1 µm). The linear gray scale range is respectively 10 nm and 10 • .

Figure 11 :

 11 Figure 11: MEB photograph of a solid bridge between two glass beads (magnification x2700, from Olivi-Tran et al 2002).

Stiction is often circumvented by the use of a sublimating fluid, such as supercritical carbon dioxide.